Abstract: This method for producing steel involves (a) a step in which a first alloy is introduced into molten steel with a dissolved oxygen amount of greater than or equal to 0.0050 mass%, (b) a step in which, after step (a), deoxidation is performed by introducing a deoxidizer into the molten steel, (c) a step in which, after step (b), a second alloy is introduced into the deoxidized molten steel, and (d) a step in which, after step (c), REM is added to the molten steel, wherein the oxygen amount Ob (mass%) brought in by the first alloy and the oxygen amount Oa (mass%) brought in by the second alloy satisfy [Oa = 0.00100], [Ob + Oa = 0.00150] and [Ob/Oa = 2.0]; after step (d), the steel satisfies the expression [0.05 = REM/T.O = 0.5].
Title of invention: Steel manufacturing method
Technical field
[0001]
The present invention relates to a method for producing steel.
Background technology
[0002]
In the steel manufacturing process, deoxidizers are used to remove oxygen, which can cause adverse effects on properties. As the deoxidizer, an element that has a strong binding action with oxygen and forms an oxide is generally used. This is because by adding an antacid to the molten steel, an oxide can be formed and oxygen can be separated from the molten steel.
[0003]
As a deoxidizer, the most common element is Al. When Al is used as an antacid, alumina, which is an oxide of Al, is formed. The above-mentioned alumina aggregates with each other to form coarse clusters (hereinafter, also referred to as “alumina clusters”).
[0004]
Such alumina clusters adversely affect the properties of the steel. Specifically, it is known that surface scratches (sliver scratches), material defects, and defects occur in steel plates such as thick plates and thin plates and steel materials such as steel pipes due to alumina clusters. In addition, the alumina cluster also causes clogging in the immersion nozzle, which is the flow path of the molten steel, during continuous casting.
[0005]
For example, Patent Documents 1 and 2 disclose a steel in which the formation of alumina clusters is suppressed without using Al as an antacid, and a method for producing the same.
[0006]
Further, as a method of detoxifying alumina clusters, a method of controlling the morphology of alumina or suppressing the formation itself by adding Ca to molten steel is used. As an example of the above method, Patent Document 3 and Non-Patent Document 1 disclose a method of modifying oxide-based inclusions such as alumina or suppressing the formation itself by using Ca.
Prior art literature
Patent documents
[0007]
Patent Document 1: Japanese Patent Application Laid-Open No. 56-5915
Patent Document 2: Japanese Patent Application
Laid-Open No. 56-47510 Patent Document 3: Japanese Patent Application Laid-Open No. 9-192799
Patent Document 4: Japanese Patent Application Laid-Open No. 2005-2425
[0008]
Non-Patent Document 1: Materials and Processes, 4 (1991), p. 1214 (Shirota et al.)
Outline of the invention
Problems to be solved by the invention
[0009]
Al is the most commonly used element as a deoxidizer in terms of manufacturing cost. Therefore, the steels described in Patent Documents 1 and 2 have a high manufacturing cost because Al is not used. Therefore, it is not suitable for mass production of steel. Further, the steels disclosed in Patent Document 3 and Non-Patent Document 1 cannot be applied to steel sheets for automobiles, and the use of steel materials is limited.
[0010]
Therefore, the present inventors investigated the formation mechanism of alumina clusters. The presence of FeO in molten steel is considered to be a factor in the clustering of alumina. Generally, the temperature of molten steel is about 1600 ° C., while the melting point of FeO is about 1370 ° C. For this reason, it has been considered that FeO is completely dissolved in the molten steel and does not exist in the molten steel, which is usually considered to have reached an equilibrium state after a sufficient time has passed.
[0011]
However, from a microscopic point of view, it is clear that there are some parts of the molten steel that have not reached the equilibrium state, and that FeO actually exists in the liquid state, even though sufficient time has passed. Became. The presence of such FeO acts as a binder for bonding alumina to each other, and contributes to the formation of coarse alumina aggregates, so-called alumina clusters.
[0012]
Therefore, it is desirable to suppress FeO in molten steel. Here, by adding a small amount of REM, which has a stronger binding action with O than Fe, the REM and O are bonded, a REM oxide is formed, and FeO in molten steel can be suppressed. it can. Based on such a FeO formation mechanism, Patent Document 4 discloses a steel in which the formation of alumina clusters is suppressed.
[0013]
On the other hand, various elements are added to steel having high level characteristics such as strength characteristics. When these elements are added to molten steel, they are added in large quantities in the form of alloys. The alloy for adjusting the chemical composition of steel in this way usually contains oxygen. Therefore, even though the formation of FeO is suppressed by using REM, when an alloy is added to adjust the chemical composition, FeO is formed again. As a result, there is a problem that the formation of alumina clusters cannot be suppressed, and surface scratches, material defects, and defects occur.
[0014]
An object of the present invention is to provide a method for producing steel, which solves the above problems, suppresses the formation of alumina clusters, and suppresses surface scratches, material defects, and defects of steel.
Means to solve problems
[0015]
The present invention has been made to solve the above problems, and the following steel manufacturing method is the gist of the present invention.
[0016]
(1) A method for producing steel, which includes
(a) a step of adding a first alloy to molten steel having a dissolved oxygen content of 0.0050% by mass or more, and
(b) after the step of (a). A step of deoxidizing by adding a deoxidizing agent to the molten steel, and
(c) a step of adding a second alloy to the deoxidized molten steel after the step (b), and
(d) the above. after the step (c),, adding an REM in the molten steel
has,
the amount of oxygen introduced by the oxygen amount and the second alloy carried over by the first alloy, the following (i) ~ (iii )
, And after the step (d) above, a method for producing steel, which satisfies the following formula (iv).
O a ≦ 0.00100 · · · (i)
O b + O a ≧ .00150 · · · (ii) O b / O a ≧ 2.0 · · · (iii) 0.05 ≦ REM / T. O ≦ 0.5 (iv) However, each symbol in the above formula is defined by the following. O B
: The amount of oxygen brought by the first alloy
(mass%) O a : amount of oxygen introduced by the second alloy
(mass%) REM: REM content
(mass%) T. O: Total oxygen content (% by mass)
[0017]
(2) The first alloy and the second alloy are one selected from metal Mn, metal Ti, metal Cu, metal Ni, FeMn, FeP, FeTi, FeS, FeSi, FeCr, FeMo, FeB, and FeNb. The steel manufacturing method according to (1) above.
[0018]
(3) The chemical composition of the steel is
C: 0.0005 to 1.5%,
Si: 0.005 to 1.2%,
Mn: 0.05 to 3.0%,
P: 0 in mass%. .001-0.2%,
S: 0.0001-0.05%,
T.I. Al: 0.005 to 1.5%,
Cu: 0 to 1.5%,
Ni: 0 to 10.0%,
Cr: 0 to 10.0%,
Mo: 0 to 1.5%,
Nb: 0 0.1%
~, V: 0 ~ 0.3%, Ti: 0 ~ 0.25%, B: 0 ~ 0.005%, REM: 0.00001 ~ 0.0020%, and T. O: The method for producing steel according to (1) or (2) above , wherein 0.0005 to 0.0050%, the balance is Fe and impurities.
[0019]
(4) The chemical composition of the steel is, in mass%,
Cu: 0.1 to 1.5%,
Ni: 0.1 to 10.0%,
Cr: 0.1 to 10.0%, and
Mo: The
method for producing steel according to (3) above, which contains at least one selected from 0.05 to 1.5% .
[0020]
(5) the chemical composition of the steel, by
mass%, Nb:
0.005 ~ 0.1%, V: 0.005 ~ 0.3%, and
Ti: 0.001 ~ 0.25%,
from The method for producing steel according to (3) or (4) above, which contains one or more selected types.
[0021]
(6) The method for producing a steel according to any one of (3) to (5) above , wherein the chemical composition of the steel is
B: 0.0005 to 0.005% in mass%
.
[0022]
(7) The method for producing a steel according to any one of (1) to (6) above, wherein the maximum diameter of the alumina cluster is 100 μm or less in the steel.
[0023]
(8) The method for producing steel according to (7) above, wherein the number of alumina clusters having a diameter of 20 μm or more is 2.0 pieces / kg or less in the steel.
Effect of the invention
[0024]
INDUSTRIAL APPLICABILITY The present invention can solve the above problems, suppress the formation of alumina clusters, and obtain a steel in which surface scratches, material defects, and defects of the steel are suppressed.
A brief description of the drawing
[0025]
[Fig. 1] Fig. 1 shows REM / T.I. It is a figure which showed the relationship between O and the maximum diameter of an alumina cluster.
FIG. 2 is a diagram showing the relationship between the amount of oxygen carried by the first alloy and the amount of oxygen carried by the second alloy in the example of the present invention and the comparative example.
Mode for carrying out the invention
[0026]
The present inventors have conducted various studies in order to reduce the generation of alumina clusters, suppress surface scratches and defects of steel materials, and improve material properties. As a result, the following findings (a) to (d) were obtained.
[0027]
(A) In order for steel to have various properties such as strength, corrosion resistance, heat resistance, and workability, it is necessary to adjust the chemical composition. Additive elements are used to adjust this chemical composition. These additive elements are usually put into molten steel in a large amount in the form of an alloy as a melting raw material.
[0028]
(B) Generally, a deoxidizing agent such as Al is added to the molten steel, and after the deoxidation of the molten steel is completed, a melting raw material having the above alloy shape for adjusting the composition of the steel (hereinafter, simply "alloy"). Also described) is put into molten steel. Since the alloy contains a small amount of oxygen, the amount of oxygen contained in the molten steel increases when a large amount of alloy is added.
[0029]
(C) The brought-in O again produces FeO in the molten steel, which causes the generation of alumina clusters. As a result, even if REM is added, FeO is formed. As described above, when a large amount of alloy is added, the formation of alumina clusters cannot be suppressed even if REM is added.
[0030]
(D) Therefore, it is effective to effectively add REM by appropriately adjusting the amount of O brought in from the alloy for adjusting the chemical composition before and after deoxidation.
[0031]
The method for producing steel according to the present invention has been made based on the above findings. Hereinafter, each requirement of the present invention will be described in detail. In the following description, the content "%" means "mass%" unless otherwise specified.
[0032]
1. 1. Outline The
present invention is a method for producing steel, and more specifically, a method for producing killed steel deoxidized by an antacid described later. Further, in the present invention, (a) a step of adding a first alloy to molten steel having a dissolved oxygen content of 0.0050% by mass or more, and (b) after the above-mentioned step (a), a deoxidizing agent is added to the molten steel. By doing so, after the step of deoxidizing, (c) after the step of (b) above, the step of adding the second alloy to the deoxidized molten steel, and (d) after the step of (c) above, It has a step of adding REM to molten steel.
[0033]
The amount of oxygen brought in by the first alloy and the amount of oxygen brought in by the second alloy satisfy the following equations (i) to (iii).
O a ≦ 0.00100 · · · (i)
O b + O a ≧ 0.00150 · · · (ii) O b / O a ≧ 2.0 · · · (iii) where the symbols in the formula It is defined by: O b : amount of oxygen brought by the first alloy (mass%) O a : amount of oxygen introduced by the second alloy (mass%)
[0034]
Further, after the step (d) above, the following equation (iv) is satisfied.
0.05 ≤ REM / T. O ≤ 0.5 (iv)
[0035]
However, each symbol in the above formula is defined by the following.
REM: REM content (% by mass)
T.I. O: Total oxygen content (% by mass)
[0036]
Hereinafter, for the sake of simplicity, the step (a) is referred to as a first alloy charging step, the step (b) is referred to as a deoxidizing step, and the step (c) is referred to as a second alloy charging step. The step (d) is referred to as a REM addition step.
[0037]
The amount of oxygen carried by the first alloy and the second alloy is defined as the total amount of O dissolved in the alloy and other O contained as an oxide.
[0038]
2. 2. Manufacturing step
(a) First alloy charging step In
the first alloy charging step, the first alloy is charged into molten steel having a dissolved oxygen content of 0.0050% by mass or more before deoxidation. As will be described later, the first alloy in this step is a general term for alloys that are added before the deoxidizing step in order to adjust the composition of molten steel. Here, the amount of dissolved oxygen in the molten steel is preferably 0.0500% by mass or less. It should be noted that the deoxidizing effect may be obtained by decarburizing before the first alloy charging step. Further, in order to make the dissolved oxygen amount of the molten steel 0.0500% by mass, an antacid may be added to the molten steel. These do not interfere with the effects of the present invention.
[0039]
Further, in the first alloy charging step, one or a plurality of alloys selected as the first alloy may be charged at one time, or may be charged in a plurality of times, and before the deoxidizing step. If so, the number of times is not particularly limited. The timing of charging the first alloy is not particularly limited as long as it is before deoxidation, but for example, in the converter, during the steelmaking of the converter, or after the steelmaking, or immediately before the vacuum degassing treatment. Alternatively, it is put into molten steel during processing.
[0040]
(B) Deoxidizing Step After the step
(a) above, that is, the first alloy charging step, deoxidizing is performed by adding a deoxidizing agent to the molten steel. The deoxidizing agent is not particularly limited, but generally, Al, Si, Zr, Al—Zr, Al—Si, or the like is used. The killed steel produced by the deoxidizer is also called Al killed steel, Zr killed steel, Al—Zr killed steel, or Al—Si killed steel. The timing of adding the deoxidizer is not particularly limited as long as it is after the first alloy is added and before the second alloy is added.
[0041]
(C) Second alloy charging step
(c) After the step (b) above, that is, after the deoxidizing step, the second alloy is charged into the deoxidized molten steel. As will be described later, the second alloy in this step is a general term for alloys that are added after the deoxidizing step in order to adjust the composition of molten steel. Further, in the second alloy charging step, one or a plurality of alloys selected as the second alloy may be charged at one time, or may be charged in a plurality of times, after the deoxidizing step. Moreover, the number of times is not particularly limited as long as it is before the addition of REM.
[0042]
(D) REM addition step
(d) After the step (c) above, that is, after the second alloy charging step, REM is added to the molten steel. In the present invention, REM is a general term for 17 elements in which Y and Sc are combined with 15 elements of lanthanoids. One or more of these 17 elements can be contained in the steel material, and the REM content means the total content of these elements.
[0043]
The REM to be added may be a pure metal such as Ce or La, an alloy of the REM metal or an alloy with another metal, and the shape may be lumpy, granular, wire or the like. In order to make the REM concentration uniform, it is desirable to add REM when refluxing the molten steel in the RH vacuum degassing tank, or to add REM while stirring the molten steel in the ladle with Ar gas or the like.
[0044]
3. 3. First alloy and second alloy
3-1. Definitions of primary alloy and secondary alloy In the
present invention, the primary alloy and the secondary alloy refer to alloys (including metals for melting raw materials) that are charged into molten steel to adjust the chemical composition of steel. As described above, the first alloy refers to the alloy charged in the first alloy charging step before deoxidation. As described above, the second alloy refers to an alloy charged in the second alloy charging step after deoxidation.
[0045]
The first alloy and the second alloy are one or more selected from metal Mn, metal Ti, metal Cu, metal Ni, FeMn, FeP, FeTi, FeS, FeSi, FeCr, FeMo, FeB, and FeNb. Is preferable.
[0046]
The above-mentioned metal Mn is a metal material for component adjustment containing Mn in a high concentration, for example, 99% by mass or more, and the same applies to metal Ti, metal Cu, and metal Ni. For example, metal Mn is defined in JIS G 2311: 1986.
[0047]
The above-mentioned "FeMn" indicates "ferromanganese". Further, for various other ferroalloys, the name of the corresponding element is added after "Fe", and for example, "ferrochrome" is described as "FeCr". Ferroalloys such as ferromanganese are defined in JIS G 2301: 1998 to JIS G 2304: 1998, JIS G 2306: 1998 to JIS G 2316: 2000, JIS G 2318: 1998, and JIS G 2319: 1998. Refers to the alloy that is used.
[0048]
3-2. Amount of Oxygen Brought in by Alloy
The first and second alloys contain oxygen, even in trace amounts. The amount of oxygen carried over from the selected alloy all as the first alloy (hereinafter, simply referred to as "amount of oxygen brought by the first alloy".) The O b to as. Further, the amount of oxygen carried over from the selected alloy all as the second alloy (hereinafter, simply referred to as "amount of oxygen brought by the second alloy".) The O a described as.
[0049]
Here, the amount of oxygen brought in from the first alloy is calculated by the following procedure. Specifically, the amount of oxygen (mass%) brought in from the specific alloy charged before deoxidation is determined by the alloy input amount (kg) x oxygen concentration in the alloy (mass%) / molten steel amount (kg). The amount of oxygen brought in from the first alloy can be calculated by calculating the values of all the oxygen amounts brought in from each alloy introduced before deoxidation according to the above calculation formula and totaling them.
[0050]
Similarly, the amount of oxygen brought in from the second alloy is calculated by the following procedure. Specifically, the amount of oxygen (mass%) brought in from the specific alloy charged after deoxidation is determined by the alloy input amount (kg) x oxygen concentration in the alloy (mass%) / molten steel amount (kg). According to the above calculation formula, the value of the amount of oxygen brought in from each alloy added after deoxidation is calculated, and by totaling them, the amount of oxygen brought in from the second alloy can be calculated.
[0051]
The first alloy and the second alloy contain oxygen. The oxygen concentration of each alloy is usually about metal Mn: about 0.5%, metal Ti: about 0.2%, metal Cu: about 0.04%, metal Ni: about 0.002%, FeMn: 0.4. %, FeP: about 1.5%, FeTi: about 1.3%, FeS: about 6.5%, FeSi: about 0.4%, FeCr: about 0.1%, FeMo about 0.01%, FeB : About 0.4%, FeNb: about 0.03%.
[0052]
The amount of oxygen carry first alloy O b and second alloys carry oxygen O a is, satisfies the following (i) ~ (iii) expression.
O a ≦ 0.00100 · · · (i)
O b + O a ≧ 0.00150 · · · (ii) O b / O a ≧ 2.0 · · · (iii) where the symbols in the formula It is defined by: O b : amount of oxygen brought by the first alloy (mass%) O a : amount of oxygen introduced by the second alloy (mass%)
[0053]
If O a exceeds 0.00100, which is the rvalue in equation (i), the formation of Al 2 O 3 and FeO cannot be suppressed. Therefore, O a , which is the lvalue of Eq. (I) , is preferably 0.00100 or less, and preferably 0.00050 or less. On the other hand, from the viewpoint of production costs O a is preferably at 0.00002 or more.
[0054]
O b and O a is the sum of the (ii) expression lvalue shall be 0.00150 or more. This is because when the lvalue of the above equation (ii) is less than 0.00150, an alloy for sufficiently adjusting the chemical composition cannot be added, and a steel having a desired chemical composition cannot be obtained. In order to effectively suppress the alumina cluster using REM, the lvalue of Eq. (Ii) is preferably 0.01700 or less.
[0055]
The lvalue of equation (iii), which is the ratio of Ob and O a , shall be 2.0 or more. This is because if the lvalue of equation (iii) is less than 2.0, the amount of alloy charged in the second alloy charging step after deoxidation becomes excessive, and the deoxidizing effect of Al or the like cannot be sufficiently obtained. The lvalue of equation (iii) is preferably 2.5 or more, more preferably 10.0 or more, and even more preferably 15.0 or more. On the other hand, when the lvalue of Eq. (iii) exceeds 130, the yield is lowered and the productivity of steel is lowered. Therefore, the lvalue in equation (iii) is preferably 130 or less.
[0056]
4. REM / T. O In the
production method according to the present invention, REM is added to the molten steel after the second alloy charging step as described above (corresponding to the REM adding step described above). In the REM addition step, REM is added to the molten steel, the mixture is sufficiently stirred, and after a lapse of time, REM and T.I. REM / T.I. O satisfies the following equation (iv).
[0057]
0.05 ≤ REM / T. O ≦ 0.5 (iv)
However, each symbol in the above formula is defined by the following.
REM: REM content (% by mass)
T.I. O: Total oxygen content (% by mass)
[0058]
FIG. 1 shows REM / T.I. It is a figure which showed the relationship between O and the maximum diameter of an alumina cluster. As is clear from FIG. 1, REM / T.I. In the range of O of 0.05 to 0.5, the maximum diameter of the alumina cluster is large and decreases. Therefore, REM / T. It is effective to adjust O so as to satisfy equation (iv).
[0059]
If the middle value of Eq. (Iv) is less than 0.05, the effect of preventing clustering of alumina particles cannot be obtained. Therefore, the middle value of Eq. (Iv) is preferably 0.05 or more, preferably 0.10 or more, and more preferably 0.20 or more. On the other hand, when the middle value of the formula (iv) exceeds 0.5, the REM becomes excessive, and this time, a cluster mainly composed of REM oxide is formed instead of the alumina cluster. , Material defects, etc. occur. Therefore, the middle value of equation (iv) is set to 0.5 or less. Further, in order to more reliably suppress the prevention of alumina clustering, the middle value of Eq. (Iv) is preferably 0.15 or more and 0.4 or less.
[0060]
Here, it is desirable to control (measure) the REM content and the total oxygen content using a molten steel sample collected after the addition of REM and after RH treatment before casting or in TD (tandish). However, if it is difficult to collect, it may be managed (measured) with a sample using a steel piece after casting. This is because it is considered that the above values do not change even after the steel pieces are formed.
[0061]
5. Chemical Composition of Steel The chemical composition of the
steel (killed steel) produced in the present invention will be described below.
[0062]
The chemical composition of the steel (killed steel) in the present invention is C: 0.0005 to 1.5%, Si: 0.005 to 1.2%, Mn: 0.05 to 3.0% in mass%. , P: 0.001 to 0.2%, S: 0.0001 to 0.05%, T.I. Al: 0.005 to 1.5%, Cu: 0 to 1.5%, Ni: 0 to 10.0%, Cr: 0 to 10.0%, Mo: 0 to 1.5%, Nb: 0 ~ 0.1%, V: 0 to 0.3%, Ti: 0 to 0.25%, B: 0 to 0.005%, REM: 0.00001 to 0.0020%, and T.I. O: It is preferable that 0.0005 to 0.0050%, and the balance is Fe and impurities.
[0063]
Steel materials such as thin plates, thick plates, steel pipes, shaped steels, and bar steels can be produced by subjecting the steel produced by the present invention to processing, heat treatment, or the like, if necessary.
[0064]
C: 0.0005 to 1.5%
C is a basic element that most stably improves the strength of steel. In order to secure the required strength or hardness, the C content is preferably 0.0005% or more. However, if the C content exceeds 1.5%, the toughness of the steel decreases. Therefore, the C content is preferably 1.5% or less. It is preferable to adjust the C content in the range of 0.0005 to 1.5% according to the strength of the desired material.
[0065]
Si: 0.005 to 1.2% If the
Si content is less than 0.005%, it becomes necessary to perform hot metal pretreatment, which imposes a heavy burden on refining and thus reduces economic efficiency. Therefore, the Si content is preferably 0.005% or more. However, if the Si content exceeds 1.2%, plating defects occur, and the surface properties and corrosion resistance of the steel deteriorate. Therefore, the Si content is preferably 1.2% or less. The Si content is preferably adjusted in the range of 0.005 to 1.2%.
[0066]
Mn: 0.05 to 3.0% When the
Mn content is less than 0.05%, the refining time becomes long and the economic efficiency is lowered. Therefore, the Mn content is preferably 0.05% or more. However, if the Mn content exceeds 3.0%, the workability of the steel is significantly deteriorated. Therefore, the Mn content is preferably 3.0% or less. The Mn content is preferably adjusted in the range of 0.05 to 3.0%.
[0067]
P: 0.001 to 0.2% If the
P content is less than 0.001%, the time and cost of the hot metal pretreatment will increase, and the economic efficiency will decrease. The P content is preferably 0.001% or more. However, if the P content exceeds 0.2%, the workability of the steel is significantly deteriorated. Therefore, the P content is preferably 0.2% or less. The P content is preferably adjusted in the range of 0.001 to 0.2%.
[0068]
S: 0.0001 to 0.05% If the
S content is less than 0.0001%, the hot metal pretreatment takes time and cost, and the economic efficiency is lowered. Therefore, the S content is preferably 0.0001% or more. However, if the S content exceeds 0.05%, the workability and corrosion resistance of the steel are significantly deteriorated. Therefore, the S content is preferably 0.05% or less. The S content is preferably adjusted in the range of 0.0001 to 0.05%.
[0069]
T. Al: 0.005 to 1.5% In the
present invention, the amount of acid-soluble Al (sol.Al) that affects the material with respect to the Al content and Al (insol.Al) derived from Al 2 O 3 which is an inclusion. ) The amount of Al, which is the total amount of the amount, is T.I. It is defined as Al (Total.Al). In other words, T.I. Al = sol. Al + insol. It means Al.
[0070]
T. If the Al content is less than 0.005%, N is trapped as AlN and the solid solution N cannot be reduced. Therefore, T.I. The Al content is preferably 0.005% or more. However, T.I. If the Al content exceeds 1.5%, the surface texture and workability of the steel deteriorate. Therefore, T.I. The Al content is preferably 1.5% or less. T. The Al content is preferably adjusted in the range of 0.005 to 1.5%.
[0071]
In addition to the above elements, one or more selected from (i) Cu, Ni, Cr and Mo, one or more selected from (ii) Nb, V and Ti, and (iii) B may be contained.
[0072]
Cu: 0 to 1.5%
Ni: 0 to 10.0%
Cr: 0 to 10.0%
Mo: 0 to 1.5%
Cu, Ni, Cr, and Mo all have hardenability of steel. It has the effect of improving and improving the strength. Therefore, it may be contained as needed. However, if Cu and Mo are contained in an amount of more than 1.5% and Ni and Cr are contained in an amount of more than 10.0%, respectively, the toughness and workability of the steel are lowered. Therefore, the Cu content is preferably 1.5% or less. The Ni content is preferably 10.0% or less. The Cr content is preferably 10.0% or less. The Mo content is preferably 1.5% or less.
[0073]
On the other hand, in order to surely obtain the strength improving effect, the Cu content is preferably 0.1% or more. Similarly, the Ni content is preferably 0.1% or more. Similarly, the Cr content is preferably 0.1% or more. Similarly, the Mo content is preferably 0.05% or more.
[0074]
Nb: 0 to 0.1%
V: 0 to 0.3%
Ti: 0 to 0.25% All of
Nb, V, and Ti have the effect of improving the strength of steel by precipitation strengthening. Therefore, it may be contained as needed. However, if Nb is contained in an amount of more than 0.1%, V is contained in an amount of more than 0.3%, and Ti is contained in an amount of more than 0.25%, the toughness of the steel is lowered. Therefore, the Nb content is preferably 0.1% or less. The V content is preferably 0.3% or less. The Ti content is preferably 0.25% or less. On the other hand, in order to surely obtain the strength improving effect, the Nb content is preferably 0.005% or more. The V content is preferably 0.005% or more. The Ti content is preferably 0.001% or more.
[0075]
B: 0 to 0.005%
B has the effect of improving the hardenability of steel and increasing the strength of steel. Therefore, it may be contained as needed. However, if B is contained in an amount of more than 0.005%, the precipitate of B may be increased and the toughness of the steel may be lowered. Therefore, the B content is preferably 0.005% or less. On the other hand, in order to obtain the effect of improving the strength of steel, the B content is preferably 0.0005% or more.
[0076]
REM: If
the REM content of the 0.00001 to 0.0020% steel is less than 0.00001%, the effect of preventing the clustering of alumina particles cannot be obtained. Therefore, the REM content is preferably 0.00001% or more. However, REM content When it is 0.0020% greater, REM object and Al oxide 2 O 3 there is a possibility that coarse clusters to generate a composite oxide having a. In addition, since a large amount of composite oxide is generated by the reaction with slag, the cleanliness of molten steel deteriorates, which may block the immersion nozzle of the tundish. Therefore, the REM content is preferably 0.0020% or less, and more preferably 0.0015% or less.
[0077]
T. O: 0.0005 to 0.0050% In the
present invention, the O content is the total amount of the solid solution O (sol. O) that affects the material and the amount of O (insol. O) present in the inclusions. , Total oxygen content is T.I. It is defined as O (Total.O). Steel T.I. If the O content is less than 0.0005%, the processing time in the secondary refining, for example, a vacuum degassing device is significantly increased, and thus the economic efficiency is lowered. Therefore, T.I. The O content is preferably 0.0005% or more.
[0078]
On the other hand, T.I. This is because if the O content exceeds 0.0050%, the collision frequency of the alumina particles increases and the clusters may become coarse. In addition, the REM required for reforming alumina increases, which lowers economic efficiency. Therefore, T.I. The O content is preferably 0.0050% or less.
[0079]
In the chemical composition of the present invention, the balance is Fe and impurities. Here, the "impurity" is a component mixed by various factors of raw materials such as ore and scrap, and various factors in the manufacturing process when steel is industrially manufactured, and is allowed as long as it does not adversely affect the present invention. Means something.
[0080]
6. Maximum diameter and number of alumina clusters
6-1. Maximum diameter of alumina clusters
steel produced by the production method of the present invention, the formation of alumina cluster is suppressed. Therefore, the maximum diameter of the alumina cluster in the steel (killed steel) is preferably 100 μm or less. This is because if the maximum diameter of the alumina cluster is more than 100 μm, the formation of the alumina cluster cannot be suppressed, and surface scratches, material defects, and defects occur in the steel material. The maximum diameter of the alumina cluster in the steel (killed steel) is more preferably 60 μm or less, and further preferably 40 μm or less. The smaller the maximum diameter of the alumina cluster, the more preferable it is.
[0081]
6-2. Number of Alumina Clusters The number
of alumina clusters of 20 μm or more per unit mass is preferably 2.0 / kg or less. This is because if the number of alumina clusters of 20 μm or more per unit mass exceeds 2.0 pieces / kg, surface scratches, material defects, and defects occur in the steel material. The number of alumina clusters of 20 μm or more per unit mass is more preferably 1.0 pieces / kg or less, and further preferably 0.1 pieces / kg or less.
[0082]
6-3. Method for measuring the maximum diameter and number of
alumina clusters The maximum diameter of alumina clusters can be measured by the following procedure. Specifically, with respect to the obtained steel (killed steel), a test piece having a mass of 1 kg is cut out from the slab, and inclusions extracted by slime electrolysis (using a minimum mesh of 20 μm) are observed with a stereomicroscope. The slime electrolysis may be any method as long as the alumina cluster can be extracted in the form existing in the steel. As an example, a constant current electrolysis of 10 A is performed in a 10% ferrous chloride solution for 5 days. Can be realized with.
[0083]
The conditions are not limited to this, for example, it was confirmed that there was no error of more than 10% in the alumina particle size as a result of preparing a steel intentionally added with artificial spherical alumina particles with a known particle size in advance and electrolyzing this. If possible, it can be said that it is suitable for the management of the present invention. Subsequently, the average value of the major axis and the minor axis of the inclusions extracted on the maximum mesh is obtained for all inclusions, and the maximum value of the average value is set as the maximum inclusion diameter, whereby the maximum diameter of the cluster is determined. Measure. Therefore, the above-measured alumina cluster may contain, for example, a slight oxide other than alumina.
[0084]
The number of alumina clusters having a diameter of 20 μm or more is measured by the following method. Specifically, similarly to the above, a test piece having a mass of 1 kg is cut out from the slab, and slime electrolytic extraction is performed. In slime electrolytic extraction, the minimum mesh is 20 μm, and the number of all inclusions of 20 μm or more observed with a stereomicroscope is converted into 1 kg unit number for measurement.
[0085]
Hereinafter, the present invention will be described in more detail with reference to Examples, but the present invention is not limited to these Examples.
Example
[0086]
The molten steel was adjusted to a predetermined carbon concentration in a 270 ton converter and put out in a ladle. A predetermined amount of the first alloy was charged at the time of steel removal or after steel removal. The molten steel that had been discharged was deoxidized using Al or the like as a deoxidizing agent in an RH vacuum degassing treatment apparatus. In addition, the second alloy was added to the molten steel after deoxidation. After adding the second alloy, REM was added to the molten steel to melt the steel. REM is Ce, La, mischmetal (for example, REM alloy consisting of Ce: 45%, La: 35%, Pr: 6%, Nd: 9%, other impurities) or an alloy of mischmetal, Si and Fe (Fe). -Si-30% REM) was added.
[0087]
Table 1 shows the content of the component adjusting metal of the alloys used as the first alloy and the second alloy and the oxygen concentration of each alloy. The alloy concentration in Table 1 refers to the content of ferroalloy or the like or the metal material for component adjustment described in the item. For example, for metal Mn, metal Ti, metal Cu, and metal Ni, the contents of these Mn, Ti, Cu, and Ni are shown, and for ferroalloy-based alloys, Si, Mn, P, S, etc., which are not Fe, etc. Indicates the content of.
[0088]
[table 1]
[0089]
Table 2 shows the amount of dissolved oxygen before the first alloy is charged, that is, before and after deoxidation, the types of the first and second alloys, and the amount of oxygen carried by the first alloy. The amount of oxygen brought in by the second alloy is described.
[0090]
Here, the amount of dissolved oxygen was measured by immersing a solid electrolyte sensor in molten steel, but it is not limited to this method. For example, from the chemical analysis results of a sample collected from molten steel, the concentration of oxides such as alumina can be calculated from the total oxygen concentration. Even if the value obtained by subtraction is used, it is considered that the same value is obtained.
[0091]
Here, the amount of oxygen brought in from the first alloy was calculated by the following procedure. Specifically, the amount of oxygen (mass%) brought in from the specific alloy charged before deoxidation was determined by the alloy input amount (kg) x oxygen concentration in the alloy (mass%) / molten steel amount (kg). .. According to the above calculation formula, the values of all the oxygen amounts brought in from each alloy introduced before deoxidation were calculated, and by totaling them, the amount of oxygen brought in from the first alloy was calculated.
[0092]
Similarly, the amount of oxygen brought in from the second alloy was calculated by the following procedure. Specifically, the amount of oxygen (mass%) brought in from the specific alloy charged after deoxidation was determined by the alloy input amount (kg) × oxygen concentration in the alloy (mass%) / molten steel amount (kg). According to the above calculation formula, the value of the amount of oxygen brought in from each alloy added after deoxidation was calculated, and by totaling them, the amount of oxygen brought in from the second alloy was calculated.
[0093]
[Table 2]
[0094]
Table 3 also shows the same items as in Table 2. The measurement was performed in the same procedure. Here, in the examples shown in Table 3, the amount of dissolved oxygen in the molten steel was 0.0050% by mass or more before deoxidation. Further, in Table 3, after deoxidation, the amount of dissolved oxygen after deoxidation is shown as a reference.
[0095]
[Table 3]
[0096]
Table 4 also shows the same items as in Table 2. In Table 4, the amount of dissolved oxygen before deoxidation is shown as in Table 2.
[0097]
[Table 4]
[0098]
Regarding the steels obtained under the conditions shown in Tables 2 to 4, the chemical composition, REM / T.I. The O ratio and the like were calculated. In the above chemical composition, REM and T.I. O was calculated from the analysis value obtained by analyzing the molten steel sample 1 minute after the addition of REM.
[0099]
As described above, the molten steel was continuously cast by a vertical bending type continuous casting machine. The casting conditions were such that the casting speed was 1.0 to 1.8 m / min and the temperature of the molten steel in the tundish was 1520 to 1580 ° C., and a continuously cast slab having a thickness of 245 mm and a width of 1200 to 2200 mm was produced. At this time, the blockage status of the immersion nozzle was also investigated.
[0100]
Specifically, after continuous casting, the adhesion thickness of inclusions on the inner wall of the immersion nozzle was measured, and the nozzle blockage status was classified into the following levels from the average value of 10 points in the circumferential direction. When the adhesion thickness was less than 1 mm, it was evaluated that there was no nozzle blockage, and it was marked with ◯ in the table. When the adhesion thickness was 1 to 5 mm, it was evaluated that the nozzle blockage had occurred slightly, and it was described as Δ in the table. When the adhesion thickness exceeds 5 mm, it is considered that nozzle blockage has occurred, and it is marked with x in the table.
[0101]
The maximum alumina cluster diameter and the number of alumina clusters of 20 μm or more per unit mass were also measured using the obtained slabs according to the following procedure.
[0102]
With respect to the obtained steel (killed steel), a test piece having a mass of 1 kg was cut out from the slab, and inclusions subjected to slime electrolytic extraction (using a minimum mesh of 20 μm) were observed with a stereomicroscope. The slime electrolysis was tested under the condition that constant current electrolysis of 10 A was carried out in a 10% ferrous chloride solution for 5 days. The magnification at the time of observation was 400 times. Therefore, the above-measured alumina cluster may contain, for example, a slight oxide other than alumina.
[0103]
The number of alumina clusters having a diameter of 20 μm or more was measured by the following method. Specifically, in the same manner as described above, a test piece having a mass of 1 kg was cut out from the slab and subjected to slime electrolytic extraction. In slime electrolytic extraction, the minimum mesh was 20 μm, and the number of all inclusions of 20 μm or more observed with a stereomicroscope was converted into 1 kg unit number for measurement. The magnification at the time of observation was 100 times.
[0104]
Then, the obtained slab is hot-rolled and pickled to produce a thick plate, and (b) hot-rolled, pickled and cold-rolled to produce a thin plate, or (c). ) Welded steel pipes were manufactured from thick plates manufactured by hot rolling and pickling. The plate thickness after hot rolling was 2 to 100 mm, and the plate thickness after cold rolling was 0.2 to 1.8 mm.
[0105]
For each of the obtained steel materials (thin plate, thick plate or steel pipe), the defect occurrence rate, impact absorption energy, and drawing value in the plate thickness direction were measured. The defect occurrence rate was calculated for each type of steel material. That is, in the case of a thin plate, the sliver scratch occurrence rate (= total sliver scratch length / coil length × 100,%) on the plate surface was calculated, and the calculated value was used as the defect occurrence rate. The sliver scratches are linear scratches formed on the surface, and a case where the sliver scratch generation rate is 0.15% or less is evaluated as a good material.
[0106]
In the case of a thick plate, the UST defect occurrence rate or separation occurrence rate (= number of defect generation plates / total number of inspection plates x 100,%) on the product plate was calculated, and the calculated value was used as the defect occurrence rate. In the case of steel pipes, the UST defect occurrence rate (= number of defect generation pipes / total number of inspection pipes x 100,%) at the welded part of the oil country tubular goods was calculated, and the calculated value was used as the defect occurrence rate.
[0107]
Here, the UST defect means an internal defect detected by using an ultrasonic flaw detector, and a case where the UST defect occurrence rate is 3.0% or less is evaluated as a good material. Further, the separation refers to a layered peeling, which was observed on the fracture surface of the test piece after the Charpy test, and the case where the separation occurrence rate was 6.0% or less was evaluated as a good material. In the table, when the generated defect is a UST defect, in the case of separation, it is described as SPR in the table.
[0108]
The UST defect was evaluated using a UST device. The UST device was an A-scope display type flaw detector, and a vertical flaw detector having an oscillator diameter of 25 mm and a nominal frequency of 2 MHz was used. In the case of thick plates, according to JIS G 0801, the case where the scratch display symbol is Δ is regarded as the occurrence of defects, and in the case of steel pipe welds, according to JIS G 0584, for the comparison test piece corresponding to the artificial flaw of category UX. When the judgment level was reached, a defect was considered to have occurred. Regarding the separation, the fracture surface was observed in the test piece after the Charpy test, which will be described later, and the presence or absence of the separation was examined.
[0109]
The above Charpy test was carried out in accordance with JIS Z 2242: 2018, and the test was carried out so that a V notch having a width of 10 mm was introduced into the test piece in the rolling direction. The test temperature was −20 ° C., and the average value of the impact values of the five test pieces was taken as the impact absorption energy.
[0110]
In the case of a thick plate, a tensile test was also performed, and the drawing value in the plate thickness direction was also calculated. The tensile test was performed in accordance with JIS Z 2241: 2011. The drawing value in the plate thickness direction is calculated by (cross-sectional area of the fractured portion after the tensile test / cross-sectional area of the test piece before the test × 100,%).
[0111]
The results obtained are summarized in Tables 5-7.
[0112]
[Table 5]
[0113]
[Table 6]
[0114]
[Table 7]
[0115]
No. that satisfies the provisions of the present invention. In A1 to A31, the generation of alumina clusters was suppressed, and the generation of defects was also reduced. In addition, No. In A1 to A31, no nozzle blockage occurred during continuous casting.
[0116]
On the other hand, No. which does not satisfy the provisions of the present invention. In B1 to B16 and C1 to C19, coarse alumina clusters were generated, and the occurrence of defects could not be reduced. In addition, No. In B1 to B16 and C1 to C19, the nozzles were slightly blocked or occurred during continuous casting.
The scope of the claims
[Claim 1]
A method for producing steel, which includes
(a) a step of adding a first alloy to a molten steel having a dissolved oxygen content of 0.0050% by mass or more, and
(b) a step of removing the first alloy into the molten steel after the step (a). A step of deoxidizing by adding an acid agent,
(c) a step of adding a second alloy to the deoxidized molten steel after the step (b), and
(d) the step (c). after the step, a step of adding a REM in the molten steel
has,
the amount of oxygen introduced by the oxygen amount and the second alloy carried over by the first alloy, the following (i) ~ (iii) formula A
method for producing steel, which is satisfied and satisfies the following formula (iv) after the step (d).
O a ≦ 0.00100 · · · (i)
O b + O a ≧ .00150 · · · (ii) O b / O a ≧ 2.0 · · · (iii) 0.05 ≦ REM / T. O ≦ 0.5 (iv) However, each symbol in the above formula is defined by the following. O B
: The amount of oxygen brought by the first alloy
(mass%) O a : amount of oxygen introduced by the second alloy
(mass%) REM: REM content
(mass%) T. O: Total oxygen content (% by mass)
[Claim 2]
The first alloy and the second alloy are one or more selected from metal Mn, metal Ti, metal Cu, metal Ni, FeMn, FeP, FeTi, FeS, FeSi, FeCr, FeMo, FeB, and FeNb. , The method for producing steel according to claim 1.
[Claim 3]
The chemical composition of the steel is
C: 0.0005 to 1.5%,
Si: 0.005 to 1.2%,
Mn: 0.05 to 3.0%,
P: 0.001 to % by mass. 0.2%,
S: 0.0001 to 0.05%,
T.I. Al: 0.005 to 1.5%,
Cu: 0 to 1.5%,
Ni: 0 to 10.0%,
Cr: 0 to 10.0%,
Mo: 0 to 1.5%,
Nb: 0 0.1%
~, V: 0 ~ 0.3%, Ti: 0 ~ 0.25%, B: 0 ~ 0.005%, REM: 0.00001 ~ 0.0020%, and T. O: The method for producing steel according to claim 1 or 2, wherein 0.0005 to 0.0050%, the balance is Fe and impurities.
[Claim 4]
The chemical composition of the steel is
Cu: 0.1 to 1.5%,
Ni: 0.1 to 10.0%,
Cr: 0.1 to 10.0%, and
Mo: 0.05 in mass%. The
method for producing steel according to claim 3, which contains at least one selected from ~ 1.5% .
[Claim 5]
The chemical composition of the steel, by
mass%, Nb:
0.005 ~ 0.1%, V: 0.005 ~ 0.3%, and
Ti: 0.001 ~ 0.25%,
is selected from The method for producing steel according to claim 3 or 4, which contains one or more of them.
[Claim 6]
The method for producing steel according to any one of claims 3 to 5 , wherein the chemical composition of the steel is
B: 0.0005 to 0.005% in mass%
.
[Claim 7]
The method for producing steel according to any one of claims 1 to 6, wherein the maximum diameter of the alumina cluster is 100 μm or less in the steel.
[Claim 8]
The method for producing steel according to claim 7, wherein the number of alumina clusters having a diameter of 20 μm or more is 2.0 pieces / kg or less in the steel.
| # | Name | Date |
|---|---|---|
| 1 | 202017056296-TRANSLATIOIN OF PRIOIRTY DOCUMENTS ETC. [24-12-2020(online)].pdf | 2020-12-24 |
| 2 | 202017056296-STATEMENT OF UNDERTAKING (FORM 3) [24-12-2020(online)].pdf | 2020-12-24 |
| 3 | 202017056296-REQUEST FOR EXAMINATION (FORM-18) [24-12-2020(online)].pdf | 2020-12-24 |
| 4 | 202017056296-PROOF OF RIGHT [24-12-2020(online)].pdf | 2020-12-24 |
| 5 | 202017056296-PRIORITY DOCUMENTS [24-12-2020(online)].pdf | 2020-12-24 |
| 6 | 202017056296-POWER OF AUTHORITY [24-12-2020(online)].pdf | 2020-12-24 |
| 7 | 202017056296-FORM 18 [24-12-2020(online)].pdf | 2020-12-24 |
| 8 | 202017056296-FORM 1 [24-12-2020(online)].pdf | 2020-12-24 |
| 9 | 202017056296-DRAWINGS [24-12-2020(online)].pdf | 2020-12-24 |
| 10 | 202017056296-DECLARATION OF INVENTORSHIP (FORM 5) [24-12-2020(online)].pdf | 2020-12-24 |
| 11 | 202017056296-COMPLETE SPECIFICATION [24-12-2020(online)].pdf | 2020-12-24 |
| 12 | 202017056296-FORM 3 [17-06-2021(online)].pdf | 2021-06-17 |
| 13 | 202017056296.pdf | 2021-10-19 |
| 14 | 202017056296-FER.pdf | 2021-10-19 |
| 15 | 202017056296-OTHERS [14-03-2022(online)].pdf | 2022-03-14 |
| 16 | 202017056296-FER_SER_REPLY [14-03-2022(online)].pdf | 2022-03-14 |
| 17 | 202017056296-DRAWING [14-03-2022(online)].pdf | 2022-03-14 |
| 18 | 202017056296-COMPLETE SPECIFICATION [14-03-2022(online)].pdf | 2022-03-14 |
| 19 | 202017056296-CLAIMS [14-03-2022(online)].pdf | 2022-03-14 |
| 20 | 202017056296-ABSTRACT [14-03-2022(online)].pdf | 2022-03-14 |
| 21 | 202017056296-US(14)-HearingNotice-(HearingDate-04-01-2024).pdf | 2023-12-06 |
| 22 | 202017056296-US(14)-ExtendedHearingNotice-(HearingDate-11-01-2024).pdf | 2023-12-12 |
| 23 | 202017056296-REQUEST FOR ADJOURNMENT OF HEARING UNDER RULE 129A [04-01-2024(online)].pdf | 2024-01-04 |
| 24 | 202017056296-US(14)-ExtendedHearingNotice-(HearingDate-07-02-2024).pdf | 2024-01-05 |
| 25 | 202017056296-FORM-26 [06-02-2024(online)].pdf | 2024-02-06 |
| 26 | 202017056296-Correspondence to notify the Controller [06-02-2024(online)].pdf | 2024-02-06 |
| 27 | 202017056296-Written submissions and relevant documents [22-02-2024(online)].pdf | 2024-02-22 |
| 28 | 202017056296-PatentCertificate12-03-2024.pdf | 2024-03-12 |
| 29 | 202017056296-IntimationOfGrant12-03-2024.pdf | 2024-03-12 |
| 1 | SearchStrategy85E202017056296(1)E_06-09-2021.pdf |