JP5333536B2 - High cleanliness bearing steel and its melting method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a high cleanliness steel with a long rolling fatigue life by controlling the oxide composition in the steel to CaO-Al<SB POS="POST">2</SB>O<SB POS="POST">3</SB>-MgO system, and a method for producing the same. <P>SOLUTION: The high cleanliness steel is characterized by including a nonmetallic inclusion which has, by mass%, C concentration of 0.85% or more and 1.2% or less; Sol. Al concentration of 0.020% or more and 0.035% or less; Cr concentration of 0.50% or more and 2.0% or less; S concentration of 0.0020% or less; and total O concentration of 0.0020% or less; and also has a circle equivalent diameter of 1.0 &mu;m or more and 10 m&mu; or less on a mirror polishing surface, when microscope observation is carried out on a sample cut from an iron slab after continuous casting and finished by mirror polishing. In the nonmetallic inclusion, Ca, Al, Mg, and O occupy 90 atom% or more among all the elements constituting the nonmetallic inclusion, and the number ratio of the nonmetallic inclusions having a CaO concentration of 20 to 50 mass% is 50% or more among all the number of the nonmetallic inclusions having a Ca concentration of 5 atom% or more. <P>COPYRIGHT: (C)2013,JPO&amp;INPIT

Description

  TECHNICAL FIELD The present invention relates to a high cleanliness bearing steel and a melting method thereof, specifically, a high cleanliness bearing steel having a long rolling fatigue life and a technology for controlling an oxide composition necessary for extending the life of rolling fatigue. About.

  Parts such as “ball bearings” and “roller bearings” that are applied to automobiles and industrial machines are subjected to repeated high surface pressure loads, and therefore are required to have an improved rolling fatigue life. In these parts, so-called inclusions in steel, such as oxides or sulfides, may become a problem, and these inclusions may be found as fracture base points on the fractured surface of a specimen that was destroyed in a rolling fatigue test. Many. For this reason, in order to improve the product performance of high cleanliness steel such as bearing steel, thorough deoxidation and desulfurization has been conventionally performed.

  O in steel often forms an oxide in molten steel and often becomes a problem as a starting point for fracture. For this reason, in order to improve a rolling fatigue life, reduction of the oxide in steel has been calculated | required. Specifically, extremely low dissolved oxygen using slag metal reaction, aggregation and levitation removal of inclusions due to reflux operation by vacuum degassing equipment, inclusions in the mold by taking a long vertical part during continuous casting For example, levitation removal promotion. As a result, the total oxygen concentration in steel, which is widely used as an index of oxide inclusions, has recently become less than 10 ppm. For this reason, in some cases, sulfide-based inclusions are discovered instead of oxide-based inclusions that have been widely discovered at the origin of destruction.

  Since S in steel is a harmful element that causes hot brittleness, desulfurization treatment has been conventionally performed by various methods. Specifically, desulfurization treatment using a mechanical stirrer in the hot metal stage, utilization of a slag metal reaction in a ladle, blowing of a desulfurization agent in a vacuum degasser, addition of Ca or Mg, and the like can be mentioned. As a result, for example, in hydrogen-resistant cracked steel that requires extremely low sulfidation, a steel material having an S concentration of less than 5 ppm can be melted.

  In such a situation, it is considered that an oxide harder than sulfides will act as a starting point for fracture, and it is divided during rolling, and the oxide is lowered and softened so that it does not act as a starting point for fracture. It is also necessary.

Here, paying attention to oxides in high clean steel, many high cleanliness steels are Al deoxidized steel, and Al ₂ O ₃ based oxides exist in the molten steel. In addition, when the refractory is melted using a ladle containing MgO, the oxide is MgO · Al ₂ O ₃ . Since these are hard, when they remain in the product stage, they are known to act as a starting point for destruction.

For example, Patent Document 1 is made of steel that satisfies JIS G4805 and is limited to O: 0.0009 mass% or less, Al: 0.005 mass% or less, and S: 0.005 mass% or less, and is rolled. The number of oxides having a size of 3 μm or more present in a cross-sectional area 160 mm ² parallel to the direction is 100 or less, of which 10 μm or more is 2 or less, and the composition ratio by composition is as follows: Alumina system: (MgO) and (SiO ₂ ) are less than 3%, and (CaO) and (CaO) / ((CaO) + (Al ₂ O ₃ )) are not more than 0.08. Spinel system: (MgO) in the range of 3% to 20%, binary system with the balance being (Al ₂ O ₃ ), 15% (CaO) and / or 15% (SiO ₂ ) mixed There is disclosed a technique relating to a high carbon chromium bearing steel in which the total number of alumina and spinel defined as having a spinel crystal structure is less than 60% of the total number of oxides.

This technology leads to a non-hard spinel system by properly selecting the slag composition during ladle refining so that hard Al ₂ O ₃ and MgO · Al ₂ O ₃ oxides are as small as possible. To do. However, since this technique is based on the premise that Al is not used as a deoxidizer, it cannot be applied to Al deoxidized steel.

In addition, Patent Document 2 describes that after adding steel to the ladle from the converter of the molten steel obtained by decarburization and refining in the converter, metal Al is added to deoxidize the molten steel in the ladle. The converter slag present on the molten steel in the ladle is discharged, and after the converter slag is discharged, the flux is added to the ladle and the basicity (CaO / SiO ₂ ) is 1.5-3 by mass ratio. 0.0 ladle slag is generated in the ladle, and then the rare gas is blown into the molten steel to stir the ladle slag and the molten steel, and then the vacuum degassing of the molten steel is performed with an RH vacuum degasser. A bearing steel melting method to be carried out is disclosed. In this document, the cause of poor rolling fatigue life of bearing steel is assumed to be non-metallic inclusions containing CaO and MgO together with Al ₂ O ₃ , and rolling fatigue life is improved by reducing these. It is going to be done.

However, the mechanism by which oxide-based nonmetallic inclusions containing CaO and MgO together with these Al ₂ O ₃ lower the rolling fatigue life has not been clarified. The disclosed melting method is within the scope of the conventional technical range, and is not a technique for intentionally manipulating the oxide composition.

Many techniques for producing hydrogen-resistant cracked steel are disclosed as clean steels with controlled inclusion composition and morphology. For example, in Patent Document 3, deoxidation by addition of Al and deoxidization and desulfurization by addition of CaO are performed on molten steel in a ladle, and then the composition of the upper surface slag in the ladle is (CaO) / (Al ₂ O ₃ ). In a state adjusted to 0.9 to 1.5, the molten steel gas is stirred, and then RH vacuum degassing is performed, and after dehydrogenation and inclusion removal, or RH vacuum degassing The manufacturing method of the clean steel excellent in the hydrogen-induced cracking-proof property which adds a CaSi powder containing wire to the molten steel in a ladle as it is and controls an inclusion form is disclosed. As shown in this document, the technology for controlling the oxide composition to Ca-based by Ca treatment after utilizing low-sulfur low-oxygen steel by utilizing powder injection desulfurization to melt clean steel is common. Is.

As a technique for controlling the oxide composition without adding an alloy, as disclosed in Patent Document 4, when the molten steel is subjected to a decompression treatment, the refractory in the decompression vessel is made of magnesia based on MgO: 40% or more, and the degree of vacuum during the treatment Has been disclosed that secures a processing time that satisfies a specific formula. In this technique, MgO in the MgO refractory is decomposed by a reduced pressure treatment, and the Al ₂ O ₃ oxide in the molten steel is changed to MgO · Al ₂ O ₃ oxide or MgO oxide.

However, this technique is a technique for modifying Al ₂ O ₃ using MgO, and does not take into account the point that the generated hard MgO · Al ₂ O ₃ -based oxide becomes the starting point of destruction at the product stage. .

Patent No. 4630075 specification JP 2008-163389 A JP-A-8-73923 Japanese Patent No. 3033000

With the recent progress in steelmaking technology, the cleanliness of high cleanliness steel including bearing steel has been greatly improved. However, in order to improve the product performance, it is necessary to control the oxide composition in addition to deoxidation and desulfurization, and in the prior art, the method of controlling the oxide composition to the MgO.Al ₂ O ₃ system has been the mainstream. . On the other hand, although problems with hard MgO.Al ₂ O ₃ -based oxides have been pointed out, the solution is mostly a reduction in oxide number density and size due to low oxygenation, which is clearly An oxide composition control method has not been shown yet.

When CaO is contained in the MgO.Al ₂ O ₃ -based oxide, it is considered that the melting point can be lowered and detoxified. However, it is sometimes confused with the oxide entrapped from the slag. That is, even if it is a soft oxide containing the same CaO, the slag-derived oxide is coarse and often found as a starting point of destruction. It has been. As the control method for CaO—Al ₂ O ₃ —MgO-based oxide, the simplest method is to add Ca directly to the molten steel. However, in steel types such as SUJ2, as described in JIS G4805, metal Ca or It was an issue of these technological developments that the Ca alloy cannot be added directly.

The present invention has been made in view of the above-mentioned problems, and its purpose is to achieve a high cleanliness with a long rolling fatigue life by controlling the oxide composition in the steel to a CaO—Al ₂ O ₃ —MgO system. In addition to providing steel, it is to provide a method for its melting.

When considering the improvement of product life, it is important to change the oxide composition from a hard MgO / Al ₂ O ₃ oxide to the basis of destruction, not to mention low oxygen and low sulfidation of steel materials. It is to reduce.

  In addition, when considering inclusion composition control, it is important to supply the Ca source into the molten steel, and in the reflux process, the Al concentration and C concentration in the molten steel are appropriate so that C deoxidation stronger than Al deoxidation dominates. And increase the degree of vacuum. That is, if the oxide can be controlled to have a composition containing CaO, the melting point of the oxide is lowered and the oxide is softened. Therefore, it is expected that the probability of acting as a starting point of destruction at the product stage is lowered.

Under the condition where C deoxidation occurs, the oxide in contact with the molten steel is reduced. The Ca source added to the molten steel exists as CaO, and most of it is considered to be absorbed by the slag. However, fine CaO exists in the molten steel, and when C deoxidation occurs, these are decomposed into Ca and O. At this time, since C deoxidation occurs in the molten steel in the vacuum chamber, the influence of CaO in the slag is considered to be limited. Believed Ca dissolved decompose in the molten steel is a MgO · _Al 2 _{O 3} based oxide in the molten steel since it is believed that the recrystallization in the nucleus, _CaO-Al 2 O 3 -MgO based oxide is generated . The oxide generated in this way is considered to be fine unlike the oxide derived from slag, and therefore the probability of reducing the product performance is low. Further, when C deoxidation occurs, the reduction reaction of not only CaO but also MgO.Al ₂ O ₃ -based oxide proceeds, so that the size of the oxide is considered to decrease.

  At this time, if the Al concentration is too high in the reflux process, if the C concentration is too low, or if the degree of vacuum is low, in the molten steel, Al deoxidation becomes dominant over C deoxidation. It is considered that there is no change in the composition of the material or the change in the size of the oxide.

As a result of the study by the present inventors based on such a situation, it has been found that the product life is significantly improved by controlling the oxide composition in the steel material to CaO—Al ₂ O ₃ —MgO system. In addition, after adding Al to the molten steel produced from the steelmaking furnace, a step of blowing a stirring gas and a desulfurizing agent into the molten steel through a bubbling lance, followed by a step of slag refining, a recirculation type degassing device The ladle refining process was sequentially performed, and the Al concentration in the molten steel in the recirculation process was optimized, and then degassing was performed under high vacuum, thereby reducing oxygen and sulfiding and controlling the oxide composition. It has been found that high-clean steel can be obtained with certainty while ensuring feasible productivity. The inventors of the present invention have completed the present invention by clarifying the conditions of Al concentration, C concentration and degree of vacuum in molten steel in the melting process and the recirculation process for controlling the oxide composition.

The present invention includes the following (1) to (3).
(1) Mass%, C concentration: 0.85 to 1.2%, Sol. Al concentration: 0.020-0.035%, Cr concentration: 0.50-2.0%, S concentration: 0.0020% or less, Total O concentration: 0.0020% or less , Si concentration: 0.1 0.8%, Mn concentration: 0.1~1.5%, P: 0.03% or less, Ca: 0.0005% or less (not including 0%) and containing organic, balance Fe and incidental inclusions together consists of things, samples the mirror polishing to a circle-equivalent diameter 1.0μm or 10μm or less nonmetallic inclusions present in said mirror surface polishing plane upon microscopic observation cut from cast piece after continuous casting Have
Of the total number of nonmetallic inclusions in which the proportion of Ca, Al, Mg and O in all elements constituting the nonmetallic inclusions is 90 atom% or more and the Ca concentration is 5 atom% or more, A high cleanliness bearing steel, wherein the number ratio of the nonmetallic inclusions having a CaO concentration of 20 to 50 mass% is 50% or more.
(2) In place of a part of the Fe, Ti: 0.005% to 0.1%, V: 0.008% to 0.3%, Mo: 0.008% to 1.0%, Nb : 0.008% to 0.1%, Ni: 0.008% to 2.0%, Cu: 1.0% or less, B: 0.0050% or less, N: 0.020% or less and wherein, (1) high cleanliness bearing steel according to item.

(3) The process of injecting stirring gas and desulfurizing agent into the molten steel through a bubbling lance, the process of slag refining, and the ladle refining with a circulating degassing device In which the Ca amount in the CaO-based desulfurizing agent blown into the molten steel through the bubbling lance is 1.0% per 1 ton of molten steel as pure Ca. -2.5 kg, and the treatment with the above-mentioned reflux type degassing apparatus was conducted at a C concentration of 0.85 to 1.2 mass%, sol. The high cleanliness described in the above item (1) or (2) , wherein the Al concentration is 0.020 to 0.035 mass%, and the degree of vacuum is 0.3 kPa or less. Method for melting bearing steel.

According to the present invention, since the probability that a hard MgO.Al ₂ O ₃ -based oxide is a starting point of fracture can be reduced, the rolling fatigue life can be extended. When used as a material for parts such as “ball bearings” and “roller bearings” that are important for automobiles and industrial machinery, safety can be improved and costs can be reduced. Moreover, since highly clean steel can be melted without significantly changing the existing steel making process, an increase in manufacturing cost can be suppressed, and the social contribution of the present invention is very large.

FIG. 1 is a graph showing the relationship between the number ratio of CaO—Al ₂ O ₃ —MgO-based oxide having a CaO concentration of 20 to 50 mass% and the rolling fatigue life. FIG. 2 is a graph showing the relationship between oxide properties and Al concentration and C concentration in the reflux process.

1. Explanation of Terms in the Present Invention “CaO—Al ₂ O ₃ —MgO-based oxide” is a nonmetallic inclusion composed of Ca, Al, Mg, and O as main constituent elements, and is attached to a scanning electron microscope. When measured with an energy dispersive X-ray analyzer or the like, it refers to an inclusion in which the proportion of the element is 90 atom% or more. On the other hand, the “MgO.Al ₂ O ₃ -based oxide” refers to an inclusion in which main constituent elements are composed of Al, Mg, and O, and the proportion of the left element is 90 atom% or more. The difference between the two is the presence of Ca in the oxide, the “CaO—Al ₂ O ₃ —MgO-based oxide” having a Ca concentration of 5 atom% or more, and the “MgO” having a Ca concentration lower than 5 atom%. “Al ₂ O ₃ oxide”. At this time, the oxide may contain 10 atom% or less of elements inevitably mixed in the refining stage such as Si, Mn, and Ti in addition to the above elements. Also, so-called sulfides or nitrides containing 45 atom% or more of S or N as a main constituent element are handled separately from oxides. These inclusions are mirror-polished samples cut from slabs 1 / 2W and 1 / 4T (W is the width and T is the thickness direction), and an observation instrument such as an optical microscope or a scanning electron microscope is used. It can be observed by using it. In the microscopic observation, a measurement visual field area of 40 mm ² or more is observed, and 20 or more inclusions having an equivalent circle diameter of 1.0 μm or more and 10 μm or less present on the mirror-polished surface are examined per sample. Since the equivalent circle diameter of more than 10.0 μm is highly likely to be an extraneous inclusion caused by slag or mold flux entrainment, it is excluded from the inspection target. At this time, a surface analysis was performed so that the entire region of the oxide was included, and from the obtained result, the composition of the oxide was changed to the content of oxides such as Al ₂ O ₃ , MgO, CaO, SiO ₂ and MnO (mass. %).

The “steel making furnace” refers to a converter or an electric furnace, and the “molten steel” produced from the steel making furnace is in a state where a primary refining process such as desulfurization, dephosphorization, or decarburization has been performed.
In the present invention, the “ladder” refers to a container used for metal refining, in which the inside of the metal iron skin is lined with bricks made of refractory. The ladle bottom is provided with a porous portion for stirring molten steel, and in the slag refining process, the molten steel and slag can be stirred by blowing gas.

  “Bubbling lance” is generally a tube in which a steel frame core is covered with a castable refractory, and a stirring gas and a desulfurizing agent can be blown into molten steel. At this time, the flow rate of the gas to be blown and the addition amount of the desulfurizing agent can be arbitrarily set.

“Stirring gas” is used for the purpose of homogenizing molten steel components and temperature, agglomeration of inclusions, promoting floating removal, hatching of ladle slag, and promoting refining reaction of molten steel and ladle slag, such as Ar Refers to inert gas. At this time, N ₂ gas, CO gas, or the like can be used in addition to Ar.

  In the present invention, the stirring operation using the stirring gas includes a stirring operation in the bubbling process and a stirring operation in the slag refining process. The stirring operation in the latter is basically a stirring operation via a molten steel stirring porous portion provided at the bottom of the ladle, but the stirring method is not limited, and the stirring operation is performed using a bubbling lance during slag refining. It is also possible.

  The “step of blowing a stirring gas and a desulfurizing agent” refers to the period from the time when the molten steel produced from the steelmaking furnace is received in a ladle to the next slag refining step and the refining operation performed there. In this refining operation, an operation of blowing a stirring gas and a desulfurizing agent into molten steel through a bubbling lance is performed.

The "slag refining process" means the period during which the so-called slag is added by adding oxides such as quick lime and silica sand, and the operation aimed at the refining reaction such as refining reaction with molten steel and heat retention Point to. In general, these medium solvents are added to the ladle to make the slag, but the slag contains CaF ₂ added to promote hatching, Al ₂ O ₃ , MgO, and FeO generated by oxidizing the molten steel components. May be included. In addition, MgO eluted from the refractory, S absorbed by the desulfurization reaction, and the residual slag from the previous smelting that has already adhered to the ladle at the time of receiving steel may be included. In slag refining, the molten steel components are adjusted by adding various alloy irons in addition to the reaction with these slags. Moreover, if it is the installation provided with the arc heating apparatus, molten steel can also be heated. Furthermore, slag refining may be performed under reduced pressure in addition to atmospheric pressure.

  The process of ladle refining with a recirculation type degassing device means that the molten steel is received in the ladle, the molten steel is sucked up into the vacuum tank by the vacuum degassing device, and the recirculating gas is flowed. This refers to the operation of recirculating the ladle and vacuum vessel and the period during which the operation is being performed. In the molten steel in the reflux, the molten steel is exposed to a reduced-pressure atmosphere, so that the degassing reaction is promoted and the inclusions are flocculated and lifted.

The “CaO-based desulfurization agent” refers to one in which main constituents of the desulfurization agent are CaO, CaF ₂ , and Al ₂ O ₃ , and pure Ca is contained in an amount of 40 mass% to 70 mass%. Inevitable impurities such as TiO ₂ , SiO ₂ , MgO and MnO may be contained at 5 mass% or less. Further, except for elements inevitably mixed in, metal elements such as Ca are not included.

2. Oxide composition and number ratio thereof In order to improve the product life, it is necessary that the nonmetallic inclusion is a CaO—Al ₂ O ₃ —MgO-based oxide. This means avoiding hard MgO.Al ₂ O ₃ -based oxides. In addition, the target CaO—Al ₂ O ₃ —MgO-based oxide requires that the production process is not caused by slag, and the number ratio of the investigation oxide should be investigated after limiting the particle size range of the investigation oxide. Can be determined. Specifically, Ca, Al among all the elements constituting the nonmetallic inclusions with respect to the total number of nonmetallic inclusions having an equivalent circle diameter of 1.0 μm or more and 10 μm or less existing within the survey area. The ratio of Mg and O is 90 atom% or more, and the CaO concentration of the non-metallic inclusions is 20 to 50 mass% out of the total number of non-metallic inclusions whose Ca concentration is 5 atom% or more. The number ratio needs to be 50% or more.

Considering the production process of oxides in steel, it can be roughly divided into oxides that are generated when deoxidizing elements are added and originally suspended in molten steel, and oxides that are generated by entraining slag and the like. Of these, the slag-derived oxide composition is considered to be close to the ladle slag composition. The present invention controls the hard MgO · Al ₂ O ₃ -based oxide originally present in the molten steel into a soft CaO-Al ₂ O ₃ -MgO-based oxide. In order to distinguish it from oxides, it is a CaO—Al ₂ O ₃ —MgO-based oxide in which the proportion of Ca, Al, Mg and O in all the constituent elements is 90 atom% or more and the Ca concentration is 5 atom% or more. It is necessary to be. In addition, among oxides satisfying the left, oxides having a CaO concentration exceeding 50 mass% are highly likely to be generated due to slag. Therefore, _CaO-Al 2 O 3 _CaO concentration -MgO based oxide is required to be less 50 mass%. On the other hand, when the CaO concentration in the oxide is 50 mass% or less, it is considered that the oxide was formed by a reaction between the oxide that was originally present and dissolved Ca. However, when the CaO concentration in the oxide is lower than 20 mass%, the oxide is not sufficiently softened, that is, the probability of acting as a fracture base point cannot be reduced. When the CaO concentration in the oxide is 20 to 50 mass%, the oxide can be expected to be softened by the CaO in the oxide, and the probability of acting as a starting point of destruction at the product stage is reduced, thereby improving the product life. it can. For this reason, the CaO concentration in the CaO—Al ₂ O ₃ —MgO-based oxide was set to 20 to 50 mass%.

  In addition, the composition control of inclusions in the present invention needs to be exerted on inclusions originally present in the molten steel. At this time, inclusions exceeding 10 μm in equivalent circle diameter increase the probability of inclusion of inclusions due to slag, so the inclusions to be investigated need to be 10 μm or less. On the other hand, if an inclusion having an equivalent circle diameter of less than 1.0 μm is investigated, the quantitativeness is insufficient. For this reason, the equivalent circle diameter of the inclusions to be investigated was set to 1.0 μm or more and 10 μm or less.

  Furthermore, in order to obtain the product performance improvement effect accompanying the softening of the oxide, it is necessary that the number ratio of the oxide having the above-mentioned size and composition is 50% or more. That is, when the number ratio of the oxides is less than 50%, the softening effect is limited and the product performance improvement effect cannot be obtained. Note that there is a correlation between the number ratio and the CaO concentration in the oxide, and it is considered that both the number ratio and the CaO concentration increase as the reducing atmosphere is stronger. If the number ratio of the oxide is 50% or more, the effect is then saturated, and therefore no upper limit is necessary.

3. Method of Melting the Steel of the Invention The method of melting the high cleanliness steel of the present invention is to blow a stirring gas and a desulfurizing agent into the molten steel through a bubbling lance with respect to the molten steel discharged from the steelmaking furnace to the ladle. The process, the process of performing slag refining, and the process of performing ladle refining with a recirculation type degassing apparatus are sequentially performed. In the following description, the above-described processes are referred to as a bubbling process, a slag refining process, and a reflux process.

The present inventors have studied in detail the melting process of high cleanliness steel, and have found the following problems and solutions.
High cleanliness steel must have low oxygen and low sulfidation, and the molten steel produced from the steel furnace is a slag refining process with slag metal reaction, degassing and inclusion agglomeration, and recirculation process that promotes floating removal. Is often applied.

In the slag refining process, slag is formed with a medium solvent having a high basicity, deoxidation and desulfurization are performed using a slag metal reaction, and the molten steel temperature and components are adjusted. However, since deoxidation and inclusion removal may be insufficient only with the slag refining process, the molten steel is cleaned by applying the recirculation process. However, when high cleanliness steel is melted by this process, the oxide composition present in the molten steel is Al ₂ O ₃ or MgO · Al ₂ O ₃ . Occasionally, an oxide with a high CaO concentration is occasionally found, but in most cases, this oxide is considered to be inevitably involved with slag during refining.

In consideration of controlling the oxide to CaO—Al ₂ O ₃ —MgO system, it is difficult to expect an oxide having a high CaO concentration due to slag that is inevitably involved, and reproducibility cannot be expected. In hydrogen-resistant cracked steel, an operation of adding an alloy containing metallic Ca to molten steel is performed to control the form of oxides. However, as described in JIS G4805, in steel types such as SUJ2, metallic Ca or Ca alloy is used. It cannot be added directly. For this reason, as another method with reproducibility, it is considered to reduce the CaO in the system to a form of dissolved Ca once and react with the MgO.Al ₂ O ₃ -based oxide that existed before that. It was. Here, as a method for reducing CaO, it was considered to use C deoxidation in the reflux step. In addition, it is necessary to consider the Ca source, but generally it is considered that the reaction between the molten steel and the slag hardly occurs during the recirculation, so it is necessary to consider a Ca source different from the CaO in the slag. It was.

  In response to this problem, attention was focused on so-called powder injection in which a CaO-based desulfurization agent is blown from a bubbling lance. Conventionally, powder injection has been a common method for deoxidation and desulfurization of clean steel, typically hydrogen-resistant cracked steel, and this process is simply applied before the slag refining and recirculation processes to remove the molten steel. If only the acid desulfurization is performed, it does not deviate from the category of the prior art.

  Here, since powder injection is a process in which CaO powder is directly added to molten steel, if CaO is added in the initial stage of refining, coarse CaO will not be contained in the system until the recirculation process in the second half of refining. We focused on the presence of fine CaO in the molten steel that is not removed by the slag refining process. That is, in addition to simply applying powder injection, when assuming C deoxidation in the reflux step, in addition to the effect of deoxidation and desulfurization, powder injection can be expected to have an effect as a process of supplying a Ca source. become.

If CaO powder is added by a vacuum degassing apparatus such as RH, a Ca source is introduced into the system. However, in this process, since the time from the addition to the pressure reduction treatment is short, coarse CaO reacts and the resulting CaO—Al ₂ O ₃ —MgO-based oxide also becomes coarse. It is expected that. For this reason, although the Ca source was introduced into the system, it was considered necessary to create a situation in which coarse CaO was removed to some extent.

In view of these, considering the most rational process for controlling the oxide to the CaO—Al ₂ O ₃ —MgO system while performing deoxidation and desulfurization, deoxidation is performed by powder injection in the bubbling process at the initial stage of secondary refining. In addition to desulfurization, the Ca source is introduced into the molten steel, and then the molten steel temperature and components are adjusted by slag refining. In the recirculation process, floating and removal of inclusions are performed, and C deoxidation is used. It can be seen that it is best to control the oxide composition. This process can be applied to a steel type such as SUJ2 because a Ca source can be introduced into the system without using metallic Ca or a Ca alloy.

4). Examination of C deoxidation in the reflux process In the present invention, it is important to utilize C deoxidation in the reflux process. Conventionally, Al deoxidation high cleanliness steel has utilized deoxidation accompanying Al addition and deoxidation accompanying slag metal reaction during slag refining. In the reflux process, Al deoxidation is often dominant, but C deoxidation may occur depending on the conditions.

However, C deoxidation occurs when the conditions of C concentration, Al concentration and vacuum degree in molten steel are satisfied. When there is no Ca source in molten steel, the oxide remains MgO.Al ₂ O ₃ system. Even if it was changed to the CaO—Al ₂ O ₃ —MgO system, the range of change was small, so C deoxidation was not fully utilized. The present invention focuses on this part.

  In the recirculation process, when the C concentration in the molten steel is lower than 0.85 mass%, it is necessary to extremely reduce the degree of vacuum in order to cause C deoxidation. is there. On the other hand, when the C concentration exceeds 1.2 mass%, C deoxidation tends to occur, but in addition to the product becoming too hard as will be described later, it is difficult to decarburize after the reflux step. For this reason, the C concentration in the molten steel in the reflux process was set to 0.85 to 1.2 mass%.

  Also, in the reflux process, when the Al concentration in the molten steel is higher than 0.035 mass%, even if the C concentration and the degree of vacuum are manipulated, the influence of Al deoxidation becomes too strong, causing a C deoxidation reaction. Is difficult. On the other hand, when the Al concentration in the molten steel is lower than 0.020 mass%, the deoxidation of the molten steel becomes insufficient, and even if C deoxidation occurs, the ratio of reacting with O in the molten steel is large, and the industrial production scale. Assuming the degassing time while maintaining the above, the frequency of the CaO decomposition reaction is small. For this reason, the Al concentration in the molten steel in the recirculation process was set to 0.020 to 0.035 mass%.

  Furthermore, in the reflux step, the degree of vacuum during processing needs to be 0.3 kPa or less. When the degree of vacuum exceeds 0.3 kPa, Al deoxidation is more dominant than C deoxidation, so that no decomposition reaction of CaO occurs. Regarding the degree of vacuum, the lower the level, the better.

5. Study on Desulfurizing Agent Composition and Addition Amount Injected in Bubbling Process The desulfurizing agent in the present invention needs to be a CaO-based desulfurizing agent. Considering desulfurization efficiency and reactivity, the CaO—CaF ₂ system is desirable, but a CaO—Al ₂ O ₃ system or a CaO—CaF ₂ —Al ₂ O ₃ system may be used. Here, the desulfurization agent shown on the left shows a difference in main constituents. In the CaO-CaF ₂ system, the total of CaO concentration and CaF ₂ concentration as main constituents is 90 mass% or more, and CaF ₂ is at least 10 mass. % Refers to those included. Similarly, the CaO—Al ₂ O ₃ system is one in which the total of CaO concentration and Al ₂ O ₃ concentration, which are main components, is 90 mass% or more, and Al ₂ O ₃ is contained at least 10 mass% or more. Point to. Further, the CaO—CaF ₂ —Al ₂ O ₃ system means that the total of CaO concentration, CaF ₂ concentration, and Al ₂ O ₃ concentration, which are main components, is 90 mass% or more, and CaF ₂ and Al ₂ O ₃ are respectively It refers to those contained at least 10 mass%.

Although there is no restriction | limiting in particular in the mixing ratio of a desulfurization agent, Ca pure content in a desulfurization agent is 40 mass% or more and 70 mass% or less by weight%, Preferably it is 55 mass% or more and 65 mass% or less. In the case where blown into the CaF ₂ in the molten steel, contributes to desulfurization to form CaS as with CaO, is believed to form fine CaO. From the viewpoint of controlling the oxide composition in the present invention, when CaO and CaF ₂ are considered as remaining Ca sources until the reflux step, both can be handled in the same manner. For this reason, the pure Ca content was calculated by dividing the Ca weight contained in CaO and CaF ₂ by the total desulfurizing agent weight.

Regarding the desulfurization agent addition amount, it is necessary to consider the amount of Ca added as a desulfurization agent to molten steel, that is, the pure Ca content of the desulfurization agent. In the present invention, it is necessary to add 1.0 kg or more per 1 t of molten steel as a pure component of Ca in the desulfurizing agent. The desulfurization rate is determined by the amount of desulfurizing agent added to the molten steel, the stirring strength and the processing time. However, when considering the shortening of the processing time of the bubbling process, the desulfurization with a pure Ca content in the desulfurizing agent of 1.0 kg / t or less. In addition to the addition amount of the agent, a sufficient desulfurization rate cannot be obtained, and the oxide composition cannot be controlled to the CaO—Al ₂ O ₃ —MgO system. On the other hand, even if a desulfurizing agent having a pure Ca content of 2.5 kg or more is added, the effect is saturated, so that an increase in the desulfurizing agent addition amount further leads to an increase in cost. In addition, when the CaO concentration in the oxide is excessively high, the melting point of the oxide is lowered, and the oxide may be coarsened. For this reason, the amount of Ca in the CaO-based desulfurizing agent in the present invention is set to a range of 1.0 to 2.5 kg / t as a pure Ca content. For this reason, the desulfurization agent addition amount is determined in consideration of the amount of Ca added to the molten steel and the pure Ca content of the desulfurization agent.

  As for the stirring gas flow rate blown in the bubbling step in the present invention, it is desirable that the stirring power density obtained from the equation (1) is 180 W / t or more. When the stirring power density is less than 180 W / t, a sufficient desulfurization rate cannot be obtained even if a large amount of a desulfurizing agent is added. On the other hand, even if a gas is blown at a stirring power density exceeding 370 W / t, the effect is saturated, and it causes an operation trouble such as molten steel blowing from the ladle. It is not necessary to increase the flow rate.

ε = (0.006183 × Q × T) / W × ln [1+ (9.8 × ρ × H) / P + {1− (TG / T)}] (1)
ε: Stirring power density per ton of molten steel accompanying gas stirring (W / t)
Q: Blowing gas flow rate (L (Normal) / min)
T: Molten steel temperature (K)
W: amount of molten steel (t)
ρ: Density of molten steel (7000 kg / m ³ )
H: Gas blowing depth (m)
P: Atmospheric pressure (N / m ² )
TG: Blowing gas temperature (K)

  Moreover, the balance between the effect of desulfurization and inclusion control and the effect of lowering the molten steel temperature is important for the processing time in the bubbling process. That is, from the viewpoint of lowering the molten steel temperature, the shorter the treatment time, the better. However, if the treatment time is too short, the effects of desulfurization and inclusion control cannot be obtained. For this reason, it is desirable that the processing time be about 5 minutes. In addition, when processing time will be 10 minutes or more, the load in post-processing, such as raising steel temperature or arc heating, will increase and it will lead to deterioration of manufacturing cost.

6). Next, the elements contained in the steel in the product stage will be described in carrying out the present invention. Hereinafter, unless otherwise noted, all are mass%.

First, the essential elements in the present invention will be described.
C: 0.85-1.2%
C is an element that governs the properties of the base metal strength, and is contained to ensure the strength and improve the rolling fatigue life. In the present invention, as described in the above item 4, in order to cause C deoxidation, the C concentration in the molten steel is required to be 0.85% or more in the reflux process. At the same time, in the present invention, the desulfurization reaction does not proceed unless the C concentration in the molten steel is high to some extent at the time of steel removal from the steelmaking furnace. On the other hand, from the viewpoint of product performance, if C exceeds 1.2%, it becomes too hard. For this reason, C concentration needs to be 0.85-1.2% or less.

Al: 0.020% to 0.035%
Al is a strong deoxidizing element and is contained to reduce the O concentration and the S concentration. In the present invention, as described in item 4 above, the sol. The Al concentration needs to be 0.020 to 0.035%. If Al is added after C deoxidation in the refluxing process, the oxide composition returns to Al ₂ O ₃ , so that Al cannot be added after the refluxing process. The Al concentration is 0.020 to 0.035%.

Cr: 0.5 to 2.0%
Cr is an element effective for improving the hardenability and improving the rolling fatigue life, and it is necessary to contain 0.5% or more. On the other hand, even if the Cr content exceeds 2.0%, the surface hardness after quenching becomes too high, the workability is lowered, and the tool life at the time of cutting is also reduced. For this reason, the Cr concentration needs to be 0.5 to 2.0%.

S: 0.0020% or less S is an element inevitably contained in the manufacturing process of steel materials. It is a harmful element that lowers strength for steel, and the smaller the content, the better. In steels with extremely reduced oxides, breakage based on sulfides occurs. For this reason, the S concentration needs to be 0.0020% or less. A desirable S content is 0.0005% or less.

O: 0.0020% or less O is an element that is inevitably contained in the manufacturing process of the steel material, and is dissolved or present as an oxide. Since it is difficult to separate the two, the O concentration in the present invention is the total oxygen concentration combining both. When the O concentration in the steel material is increased, the amount of oxide is increased, so that the probability that the steel material is broken is increased. For this reason, Total. The O concentration needs to be 0.0020% or less. Desirable Total. The O content is 0.0005% or less.

Subsequently, elements other than the above that constitute the highly clean steel will be described.
Si: 0.1 to 0.8%
Si acts as a deoxidizing element in molten steel, and is useful for increasing the hardenability and improving the rolling fatigue life in steel, and it is desirable to contain 0.1% or more. On the other hand, even if Si is contained in excess of 0.8%, the effect of improving quenching is saturated, and the base material becomes hard and the tool life during cutting is reduced. For this reason, the Si concentration is desirably 0.1 to 0.8%.

Mn: 0.1 to 1.5%
Mn is useful as a deoxidizing agent, and is useful for increasing the hardenability of the steel material and increasing the machinability of the steel material by forming MnS in the steel material, and contains 0.1% or more. It is desirable. On the other hand, even if it contains Mn exceeding 1.5%, the above effect is saturated. For this reason, it is desirable that the Mn concentration is 0.1 to 2.5%.

P: 0.03% or less P precipitates at grain boundaries and lowers the toughness and ductility of the steel material. If the P content exceeds 0.03%, the rolling fatigue life is significantly reduced. Therefore, the P concentration is preferably 0.03% or less.

Ca: 0.0005% or less (excluding 0%)
Ca is an element that is inevitably contained from a solvent medium or the like in the production process of steel, and may be contained in oxides and sulfides. When Ca is contained in the oxide, the oxide has a low melting point, and the probability that becomes the starting point of destruction of the steel material is lowered. Similarly, when Ca is contained in the sulfide, the probability that the base material for the destruction of the steel material is reduced. In the present invention, the oxide must be CaO—Al ₂ O ₃ —MgO, and therefore should not be O%. The amount of Ca in the inclusion is very small, and if it is 0.0005% or less, it will not be a big problem. However, when the Ca content exceeds 0.0005%, the oxide becomes coarse, leading to a reduction in rolling fatigue life. For this reason, it is desirable that the Ca concentration is 0.0005% or less (not including 0%).

  The high cleanliness bearing steel according to the present invention contains the above-described C, Si, Mn, P, S, Cr, Al, S, Ca, O, and is composed of the remaining Fe and inevitable inclusions. In addition to the above, for the purpose of adding functions necessary for the product, Ti: 0.005% to 0.1%, V: 0.008% to 0.3%, instead of a part of the Fe , Mo: 0.008% to 1.0%, Nb: 0.008% to 0.1%, Ni: 0.008% to 2.0%, Cu: 1.0% or less, B: 0.0050 % Or less, N: 0.020% or less may be included.

  Steels having the compositions shown in Table 1 were melted. The amount of molten steel was about 80 t, and a bubbling process, a slag refining process, and a reflux process were sequentially performed. At this time, as a comparative example, a process in which the bubbling process was omitted was also performed. Table 1 summarizes the steel components of the present invention and comparative examples. In the refining stage, the hot metal discharged from the blast furnace was desulfurized by hot metal pretreatment, de-P and de-C treated in a converter type refining vessel (CV, Converter), and then received in a ladle. When receiving the steel in the ladle, the converter slag was prevented from entering the ladle, an alloying element containing Al was added to the molten steel, and a cover slag for heat insulation was added.

  After the molten steel in the ladle was transported to PI (Powder Injection, powder addition device), Ar gas was blown into the molten steel while adding a desulfurizing agent via a bubbling lance, and the molten steel was stirred. The molten steel processing time in the bubbling process at this time was about 5 minutes, and the desulfurizing agent addition amount to be blown in was varied.

Then, the process with a slag metal reaction was performed in VAD (Vacuum Arc Degassing), and the molten steel composition and molten steel temperature were adjusted. At this time, with the intention of promoting deoxidation and desulfurization, the solvent was adjusted so that CaO, CaF ₂ , Al ₂ O ₃ were the main constituents and the CaO / Al ₂ O ₃ ratio was about 3. Was added. In VAD, it was processed for about 40 minutes, during which the molten steel temperature was changed from about 1550 ° C to 1580 ° C. Further, degassing and inclusion removal were performed with an RH (circulating vacuum degassing apparatus). The treatment time with RH was approximately 40 minutes, and the treatment of circulating the molten steel in a state where the degree of vacuum was the lowest was performed for 25 minutes to 30 minutes. At this time, the molten steel temperature changed from approximately 1520 ° C to 1550 ° C. Then, it cast by the continuous casting method and obtained the slab of 300 mm x 400 mm size.

  A molten steel sample collected at the end of the bubbling process, slag refining process, and recirculation process, and a block sample and chips for analysis were collected from the obtained slab, and subjected to chemical analysis. Further, a micro sample for observing inclusions was cut out from the ½ W and ¼ T parts (W is the width and T is the thickness direction) of the slab. The inclusion observation micro sample was filled with resin and then mirror polished, and the oxide in the sample was observed with a scanning electron microscope to investigate the oxide composition.

  At this time, when measured with an energy dispersive X-ray analyzer attached to the scanning electron microscope, the CaO concentration is mass% in inclusions present in one sample with an equivalent circle diameter of 1.0 μm to 10 μm. The ratio (%) of the oxide containing CaO in the slab sample was calculated by dividing the number of oxides contained by 20% or more by the total number of oxides observed.

  The obtained slab was held in a soaking furnace at 1200 ° C. and then cracked and rolled at a temperature range of 1020 ° C. to 1100 ° C. to obtain a steel slab of 160 mm × 160 mm. The steel slab was heated to 1050 ° C. and then rolled in a temperature range of 800 ° C. to 930 ° C. to obtain a steel bar having a diameter of 70 mm. At this time, the reduction was applied so that the total reduction ratio was 15 or more and the reduction ratio in the temperature range of 1000 ° C. or more was 4 or more. A spheroidizing annealing process (furnace cooling after holding at 780 ° C. for 6 hours) is applied to the steel bar having a diameter of 70 mm, and then sliced so that the longitudinal direction becomes the thickness of the shaped material, and the diameter is 60 mm. A shaped material having a thickness of 5.5 mm was collected. This shaped material was heated at 830 ° C. for 30 minutes, then quenched with oil, further heated at 180 ° C. for 1 hour, and then tempered by being allowed to cool in the air. A rolling fatigue test piece was created by lapping the surface of this raw material and subjected to a rolling fatigue test.

  Table 2 shows the rolling fatigue test conditions. The rolling fatigue test was performed using a thrust type rolling fatigue tester under conditions of a repetition rate of 1800 cpm (cycle per minute) and a maximum contact surface pressure of 5230 MPa. The rolling fatigue test results were plotted on the Weibull distribution probability paper, and the L10 life showing 10% failure probability was evaluated as the rolling fatigue life.

Table 3 shows the melting conditions and the investigation results of the C concentration, Al concentration, vacuum degree, oxide composition, and fatigue life of the present invention and the comparative example in the reflux process.
Of the values shown in Table 3, the relationship between the number ratio of CaO—Al ₂ O ₃ —MgO-based oxide containing 20% or more of CaO and the fatigue life is shown in a graph in FIG. As shown in the graph of FIG. 1, according to the present invention, the oxide composition is changed to a soft CaO—Al ₂ O ₃ —MgO system, and when the number ratio is 50% or more, the rolling fatigue life is improved. I understand that.

Among the values shown in Table 3, the amount of Ca in the desulfurizing agent is 1.0 to 2.5 kg / t, and the vacuum level in the reflux step satisfies 0.3 kPa or less. FIG. 2 is a graph showing the relationship between the Al concentration and the C concentration. The white circles in the figure indicate that the ratio of CaO—Al ₂ O ₃ —MgO-based oxide containing 20% or more of CaO is 50% or more, and the triangles indicate CaO—Al ₂ containing 20% or more of CaO. The ratio of the O ₃ —MgO-based oxide was lower than 50.

  As can be seen from the graph of FIG. 2, the composition of the oxide under conditions where the Al concentration in the molten steel in the reflux process is 0.020 to 0.035% and the C concentration in the reflux process is 0.85 to 1.2%. It can be seen that control is possible. Here, even if the Al concentration and the C concentration are within the range of the present invention, when the degree of vacuum is 0.3 kPa or less, the oxide composition cannot be controlled. Further, when the bubbling process is not performed or the Ca content in the desulfurizing agent is less than 1.0 kg / t, the composition control of the oxide cannot be performed. From this, the oxide composition is controlled by adding a sufficient Ca source in the bubbling process, adjusting the Al concentration and C concentration in the molten steel so that C deoxidation occurs, and reducing the degree of vacuum. It can be seen that it is necessary to

Claims (3)

mass%, C concentration: 0.85 to 1.2%, Sol. Al concentration: 0.020-0.035%, Cr concentration: 0.50-2.0%, S concentration: 0.0020% or less, Total O concentration: 0.0020% or less , Si concentration: 0.1 0.8%, Mn concentration: 0.1~1.5%, P: 0.03% or less, Ca: 0.0005% or less (not including 0%) has free and the balance Fe and incidental inclusions together consists of things, samples the mirror polishing to a circle-equivalent diameter 1.0μm or 10μm or less nonmetallic inclusions present in said mirror surface polishing plane upon microscopic observation cut from cast piece after continuous casting Have
Of the total number of nonmetallic inclusions in which the proportion of Ca, Al, Mg and O in all elements constituting the nonmetallic inclusions is 90 atom% or more and the Ca concentration is 5 atom% or more, A high cleanliness bearing steel, wherein the number ratio of the nonmetallic inclusions having a CaO concentration of 20 to 50 mass% is 50% or more. In place of a part of the Fe, Ti: 0.005% to 0.1%, V: 0.008% to 0.3%, Mo: 0.008% to 1.0%, Nb: 0.0. 008% to 0.1%, Ni: 0.008% to 2.0%, Cu: 1.0% or less, B: 0.0050% or less, N: 0.020% or less The high cleanliness bearing steel according to claim 1 . A process of blowing stirring gas and desulfurizing agent into molten steel through a bubbling lance, a process of slag refining, and a process of refining a ladle with a recirculation type degassing device for the molten steel that has been delivered to the ladle from a steelmaking furnace Is a method for melting high cleanliness bearing steel,
The amount of Ca in the CaO-based desulfurizing agent blown into the molten steel through the bubbling lance is 1.0 to 2.5 kg per 1 ton of molten steel as a pure Ca component , and
The treatment with the recirculation type degassing apparatus was carried out in such a manner that the C concentration in the molten steel was 0.85 to 1.2 mass%, sol. The high cleanliness degree according to claim 1 or 2, wherein the Al concentration is 0.020 to 0.035 mass% and the degree of vacuum is 0.3 kPa or less. Method for melting bearing steel.

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