1. Technical Field
The present invention relates to a method for producing a carburized part by carburizing a steel member under a vacuum.
2. Background Art
Carburization treatment for improving strength of a surface of steel materials is conventionally performed by a method such as gas carburization and vacuum carburization. For example, in gas carburization, as a method for improving a carburizing property by a preliminary oxidation, a method for carburizing a high-alloy steel after a preliminary oxidation (Japanese Unexamined Patent Application Publication No. 50-1930), and a method for carburizing under reduced pressure after a preliminary oxidation (Japanese Unexamined Patent Application Publication No. 9-324255) are known. Moreover, as a method for producing a carburized part under reduced pressure, a method for carburizing and nitriding in succession in a decompression furnace (Japanese Unexamined Patent Application Publication No. 2006-28541), a method for rapidly carburizing under reduced pressure by using ethylene gas (Japanese Unexamined Patent Application Publication No. 11-31536), and a method for rapidly carburizing under reduced pressure by feeding carburizing gas in pulses (Japanese Unexamined Patent Application Publication No. 2004-332074) are known. Furthermore, as a method for partially carburizing or for partially changing a depth or a concentration of carburization, a method for partially carburizing by using an anti-carburizer (Japanese Unexamined Patent Application Publications No. 10-273771 and No. 4-32537), a method for partially carburizing by using a plating (Japanese Unexamined Patent Application Publication No. 8-60335), a method for controlling a depth of carburization by utilizing a plastic deformation (Japanese Unexamined Patent Application Publication No. 5-25610), and a method for removing unnecessary portions by grinding or cutting after high concentration carburization (Japanese Unexamined Patent Application Publication No. 4-250927) are known.
In gas carburization, an intergranular oxidation layer is formed on a surface of a steel material, and it functions as an initial crack, whereby fatigue strength may be decreased. Moreover, elements effective for quenching are oxidized, and metallic structure is insufficiently quenched, whereby pitting strength may be decreased. On the other hand, carburization under reduced pressure (a vacuum) is a method effective for improving pitting strength because the intergranular oxidation layer is not formed. However, the cost of equipment for reducing pressure is high, and therefore, a method for carburizing as rapidly as possible is required. Properties of some products may be improved by partially carburizing, but both the gas carburization and the decompressed carburization using conventional techniques take substantial amounts of time and effort.
An object of the present invention is to provide a method for producing a carburized part. In the method, decompressed carburization can be rapidly performed, thereby reducing processing time and amount of carburizing gas used. Moreover, a product having partially different concentration of carburization is easily obtained by the method.
An oxide film formed on a surface of a steel member was thought to retard carburization treatment. However, the inventors have found that an oxide film having a certain range of thickness actually accelerates the carburization reaction occurring during decompressed carburization, and the present invention has thereby been completed. That is, the present invention provides a method for producing a carburized part by carburizing a steel member under a vacuum in a decompression furnace feeding carburizing gas. The method comprises a step for forming an oxide film on at least a part of a surface of the steel member, a step for generating carbon by reducing the oxide film with the carburizing gas, and a step for carburizing the surface of the steel member under a vacuum by diffusing the carbon. In the present invention, the thickness of the oxide film is preferably adjusted to be in a range of 0.05 to 5 μm.
According to the present invention, carburization under reduced pressure can be accelerated, whereby carburization time and running cost are reduced, and high concentration carburization is easily performed. Moreover, partial carburization, which is difficult to perform by conventional techniques, can be easily performed by the present invention.
First, a function of the present invention will be described.
1. Carburization Reaction with Hydrocarbon
Carburization reaction with hydrocarbon such as propane, ethylene, acetylene, and the like proceeds under a reduced-pressure atmosphere according to diffusion of carbon produced by decomposition of hydrocarbons.
In the case of decompressed carburization, whereas gas is continuously drawn by a vacuum pump, hydrocarbons for carburization are fed. Therefore, the above reaction will not be in an equilibrium state, and the carburization reaction continuously proceeds. Specifically, in a reduced pressure atmosphere, a method called “pulse carburization”, in which carburizing gas is intermittently fed, is often used, and it is important to accelerate the carburization reaction while the carburizing gas is fed. In this case, a means for improving a rate of carburization is examined from a viewpoint of a free-energy change. The free-energy change in the formula 1, “ΔG1”, is defined by the following formula.
ΔGx0: free energy of formation of X
R: gas constant
T: temperature
In this case, “K1” represents a ratio of concentration in the formula 1.
pC
pH
aC: concentration (activity) of C
ΔGC0=0, ΔGH
ΔG1=−ΔGC
The reaction of the formula 1 occurs when ΔG1 is negative, and it can be accelerated by adjusting ΔG1 to a negative value that is as low as possible. Therefore, it is effective to adjust K1 to a small value and to adjust T to a large value. That is, in a condition of decompressed carburization, K1<1, and RTlnK1 becomes a negative value according to the following formula.
pC
In order to set K1 to a small value, according to the formula 3, it is effective to increase the partial pressure of the hydrocarbon and to decrease the partial pressure of hydrogen. However, the improvement of these conditions is limited under the conditions of the decompressed carburization.
The effect of the increasing of T, that is, raising temperature, is generally known, but the temperature should be set to 1000° C. or higher so as to further reduce carburization time, and various undesirable effects thereby follow. For example, if an allowable temperature limit of a furnace of a carburization device is to be improved, the design of the device must be substantially modified. In addition, the service life of a heater may be decreased, and maintenance must be frequently performed, whereby an operation rate is decreased. Moreover, effects on an object to be carburized cannot be avoided. That is, properties of a steel material may deteriorate because crystal grains of the steel material become coarser, and strain is increased during heat treatment. Thus, reducing of carburization time by raising the temperature has disadvantages.
In surface treatment and surface modification as represented by carburization, an oxide film is generally supposed to be an obstruction, and it is removed as much as possible. This is because the oxide film functions as a barrier film during a surface treatment, and it often undesirably affects a reaction and an adhesion at a surface. However, the inventors have found that an oxide film formed before carburization accelerates carburization during decompressed carburization. The function will be described by using reaction formulas.
Carburization reaction when an oxide film FexOy exists is represented by the following formula.
Free energy change ΔG8 of the formula 8 can be defined by the following formula.
In this case, K8 is represented by the following formula.
pH
aFe: concentration (activity) of Fe
aFe
In this case, a condition under which the reaction of the formula 8 proceeds more than the reaction of the formula 1 has been investigated. In this condition, ΔG1 in the formula 6 and ΔG8 in the formula 9 are used so as to obtain a relationship of ΔG1>ΔG8. Then, this condition is rewritten as follows.
ΔG1−ΔG8>0
In this case, the above condition can be represented by the following formula according to the formulas 6 and 9.
The formulas 3 and 10 are substituted for the formula II so that K1/K8 can be represented by the following formula.
In this case, if a degree of vacuum is maintained, the following formula 13 can be assumed, whereby the formula 12 is represented by the following formula 14.
The formula 14 is substituted for the formula 11, and the following formula is obtained.
In this case, a member to be carburized is assumed to be completely covered with an oxide film, and the formula 15 is calculated by using the following formulas.
aFe
aFe=0 (17)
As a result, the second term of the formula 15 diverges to infinity, thereby satisfying ΔG1−ΔG8>0. That is, carburization can be accelerated regardless of temperature, the type of carburizing gas, and the type of oxide film. This condition is obtained when an ordinary oxidation treatment is performed, and every carburizing gas may have the effect (It should be noted that m>0).
Assuming that an oxide film includes some defects, the formula 15 is calculated in a condition in which the oxide film is 99% and iron-based material is 1%. In this example, ethylene (C2H4) is used as carburizing gas, and Fe2O3 is used as the oxide film.
ΔGFe
ΔGH
Since m=4, and y=3, the first term of the formula 15 will be 7 kJ/mol. The second term will be 99 kJ/mol according to the following formulas.
aFe
aFe=0.01 (21)
Therefore, ΔG1−ΔG8=106 kJ/mol, thereby satisfying ΔG1−ΔG8>0. According to this calculation, ΔG1−ΔG8 is calculated with respect to gas used in practice in decompressed carburization, and the results are shown in Table 1. As shown in Table 1, every condition satisfies the relationship of ΔG1−ΔG8>0.
It should be noted that the following formula represents coverage in a micro region of an oxide film, and it is not a macro-area ratio of an oxide film on a surface of a portion to be carburized.
aFe
In an investigation of a chemical reaction, a probability of encountering reactive molecules within a mean-free path of molecules of carburizing gas (a moving distance in which the molecule travels between collisions with other moving molecules) is important, and a concentration and a coverage are parameters that should be considered from this point of view.
According to the above theoretical consideration, the existence of an oxide film accelerates carburization reactions occurring during decompressed carburization.
As described above, the existence of an oxide film accelerates carburization reactions. An oxide film with several nanometers thick may practically be formed simply by disposing a steel material in the atmosphere before carburization, and this is according to the following formula.
aFe
Such an oxide film has no effect because when a carburization treatment is started, the oxide film is reduced according to the reaction of the formula 8, and the abundance of the oxide film is thereby suddenly decreased. Therefore, in order to obtain an effective oxide film in a real operation, a certain amount of the oxide film is required so that the oxide film is maintained during the real operation without depletion, that is, a certain thickness of oxide film is required. On the other hand, the oxide film substantially functions as a barrier film. If the oxide film has a sufficient thickness to prevent the diffusion step of carbon to a large degree, the carbon, which is produced, cannot diffuse, whereby they remain at a surface of a steel material as “soot”.
As described above, the effect of the present invention may not be obtained when the oxide film is too thin, and the oxide film may function as an obstruction to carburization when it is too thick. Therefore, there may be a suitable thickness of the oxide film that is formed preliminary. The inventors have repeatedly experimented and found the optimum conditions for forming an oxide film, and the range of the optimum conditions will be described hereinafter.
In the present invention, the effect can be obtained by using every steel regardless of its compositions. In this case, an example of using a steel defined by JIS SCM420H, which is generally used as a steel to be carburized, will be described. The chemical composition of a material used in the experiments is shown in Table 2.
This material was normalized under the conditions shown in
Next, thickness of an oxide film on the surface of each specimen was measured by the following method. A specimen having film thickness of 0.1 μm or more was polished at the cross section, and a distribution state of oxygen was analyzed at the cross section by a line analysis of EPMA (Electron Probe X-ray Micro Analyzer). According to a distribution curve shown in
Then, these specimens were carburized under the conditions shown in
The specimen carburized thus was cut off, and the section was analyzed by the line analysis of EPMA so as to measure a depth distribution of carbon concentration. The depth distribution of carbon concentration showed distribution characteristics as shown in
According to the results shown in Table 4, the diffusion depth of carbon is not much changed with respect to the change in the thickness of oxide films, but the carbon concentration at the surface and the effective depth of the hardened layer are changed. As estimated above, this indicates that the oxide film accelerates the carburization reaction of the surface. On the other hand, the diffusion depth may represent the effect of diffusion time during carburization treatment rather than the effect of the oxide film. Since the effective depth of the hardened layer depends on the carbon concentration at an intermediate point between the surface and the diffusion depth, it is affected by the carbon concentration at the surface, whereby it is affected by the thickness of the oxide film.
The inventors have investigated whether or not carburization is accelerated by a relationship of the carbon concentration at the top surface and the thickness of an oxide film formed by preliminary oxidation. As shown in Table 4, when the thickness of the oxide film is 0.05 μm or more, there is an accelerating effect for carburization. When the oxide film has thickness of more than 5 μm, it functions as a barrier film and inhibits carburization. Therefore, a suitable thickness of the oxide film in the present invention is 0.05 to 5 μm. Specifically, when the thickness of the oxide film is in a range of 0.2 to 3.5 μm, the oxygen concentration at the surface is extremely improved, and a great effect can be obtained.
In the above experiments, the accelerating effect for carburization was verified by using carbon concentration as a parameter under conditions in which the carburization time was fixed. In order to form a carburized part having a carbon concentration at the same level as that of a portion formed by conventional techniques, carburization can be performed in short periods by using the present invention, whereby the running cost, particularly, the amount of carburizing gas used, can be reduced.
According to the results shown in Table 4, the accelerating effect for carburization is obtained when the temperature is not more than 550° C., but the carburization is inhibited when the temperature is 600° C. This is because FeO is formed inside the oxide film when the temperature is 570° C. or higher, and the film may grow and become thick, whereby the oxide film effectively functions as a barrier with respect to the diffusion of carbon. However, when carburization is performed under conditions in which the thickness of an oxide film is decreased by removing the top surface of the oxide film using a surface treatment such as a shot blasting after preliminary oxidation is performed at 570° C. or higher, the accelerating effect for carburization can be obtained. Accordingly, the thickness of an oxide film is more important than the temperature of oxidation, but in order to avoid additional steps, the temperature of preliminary oxidation is preferably set at 250 to 550° C.
In a conventional technique that is thought to be similar to the present invention, it is known that a preliminary oxidation is effective as a pretreatment for gas carburization for high-alloy steel such as stainless steel (see Japanese Unexamined Patent Application Publication No. 50-1930). In this case, the purpose of the preliminary oxidation is to decrease a function of an oxide film as a barrier during gas carburization by forming a thick oxide layer so that the oxide layer may break away and be porous. Therefore, the preliminary oxidation disclosed in the conventional technique is completely different from the treatment of the present invention, which is designed to accelerate carburization during decompressed carburization. In Japanese Unexamined Patent Application Publication No. 50-1930, oxidation is preferably performed at 1800° F. (approximately 985° C.) for 0.5 to 1 hour, and the conditions are obviously different from the conditions of the present invention.
An oxide film does not break away at a temperature within the above range and grows parabolically, and the time of heat treatment can be selected within the time estimated by the following formula.
d=√{square root over (k2t+d02)} (24)
d: film thickness
d0: initial film thickness (film thickness naturally produced)
k: rate constant
t: time
In general, since d0 is very small with respect to a film produced by oxidation, it is approximated to 0. For example, as shown in Table 3, when the temperature is 300° C., t=60 minutes and d=0.39, whereby k can be estimated to be 0.050 (in this case, d0=0). Since the maximum thickness of an oxide film having an effect in the present invention is 5 μm, the time for producing an oxide film of 5 μm can be calculated to be 4.9×103 minutes (in this case, d0=0) according to the following formula.
The examples of the present invention shown in Tables 3 and 4 show results of oxidation in air. Whether oxides are produced or not depends on the oxygen partial pressure. For example, as shown in the examples of the present invention, when the temperature is 550° C., the equilibrium oxygen partial pressure of Fe2O3 is approximately 10−11 Pa (10−16 atm), and therefore, the oxygen partial pressure should be higher than 10−111 Pa. In order to accelerate the oxidation reaction, a higher oxygen partial pressure is preferable, and an oxygen partial pressure of 10 Pa (10−4 atm) or more is more preferable. Such an oxygen concentration can be formed in the air without any atmosphere control, and no limit is specified. It should be noted that when H2 or CO coexists, the present invention can be performed in a condition in which the oxygen potential is at not less than a degree corresponding to 10−11 Pa (10−16 atm).
For example, when the following reaction occurs at 550° C., by setting the ratio of partial pressures according to the formula 27, the oxygen partial pressure can be represented as the formula 28.
As a method for obtaining effects by gas carburization, a method is disclosed in Japanese Unexamined Patent Application Publication No. 9-324255 in which gas carburization performed after preliminary oxidation is performed at an oxygen partial pressure of 10−14 to 10 Pa (10−19 to 10−4 atm). In this case, the temperature of preliminary heat treatment is 750° C., and the dissociation oxygen partial pressure of Fe2O3 is 10−5 Pa (10−10 atm), whereby a stable oxide film cannot be formed when the oxygen partial pressure is 10−5 Pa or less. In this document, since the amount of formed oxide film is not disclosed, some effects of modifying a surface, such as removal of oil adhering to a surface under a high vacuum of 10−19 to 10−4 atm (10−14 Pa to 10 Pa), may be larger than the effect of forming an oxide film. Therefore, an oxide film having a thickness that is required in the present invention cannot be obtained by the method disclosed in the above document, and the above preliminary oxidation does not have an effect as a pretreatment for decompressed carburization.
In general, all kinds of steel may be used as the steel material to be carburized. In a case of a steel material including Cr of not less than 10%, a spinel-type oxide (FeO.Cr2O3) is mainly formed, and a growth rate of film thickness differs from that of a case in which ferrioxides are mainly formed, whereby suitable oxidation conditions also differ therefrom. In this case, the oxide film also has an accelerating effect on carburization, and the present invention can be used. Specifically, since a steel material including Cr at not more than 10% such as carbon steels, SCR materials (chrome steels), SCM materials (chrome molybdenum steels), SNC materials (nickel chrome steels), and SNCM materials (nickel chrome molybdenum steels) form an oxide film primarily containing ferrioxides, the present invention can be used, and the object of the present invention can be achieved under the conditions of preliminary oxidation shown in the examples.
In a method of preliminary oxidation, as shown in
On the other hand, as a method that is different from the above method, as shown in
The above-described methods are examples for performing the present invention, and a method can be selected according to the purposes, the formations of furnaces in operation, the amount of circulation, and the like.
When carburizing gas is represented by CnHm, as shown by the formula 15, if m>0, the accelerating effect for carburization can be obtained regardless of the kind of carburizing gas (the value of n and m). That is, the effects of the present invention can be obtained by using hydrocarbons such as methane, ethane, propane, butane, ethylene, and acetylene, or carburizing gas including H in its molecular structure such as oil vapors, alcohols, and natural gases. In this case, in order to accelerate the reaction shown by the above formula 8 in the present invention, hydrocarbon gases represented by CnHm are the most suitable. According to the formula 15, the effects increase with smaller m (in this case, m>0). Since hydrocarbon gas having m=1 does not exist, hydrocarbons having m=2 to 6, such as propane (m=6), ethylene (m=4), and acetylene (m=2) are effective. When carburizing gas having m=0 is used, the effects of the present invention cannot be obtained. For example, in a case of using CO or CO2, the effects of the present invention cannot be obtained.
Theoretical background for explaining that the effects of the present invention can be obtained at any temperature of carburization, and the calculation results (Table 1) based thereon have already been described. An oxide film having a suitable thickness disclosed in the present invention has the effects even when the carburization temperature is changed. The minimum thickness of an oxide film limits the time required for reducing the oxide film, which is a part of the total time of the carburization reaction. When the total time of the carburization reaction is changed by changing the carburization temperature, the time required for reducing an oxide film is also changed at the same rate, whereby the ratio of both times is constant even when the temperature is changed. The above case can be applied to a case of the maximum thickness of an oxide film. The maximum thickness of an oxide film is defined by the barrier property with respect to the diffusion of carbon during carburization. When the diffusion property of carbon is changed by the change of the temperature, the amount of carbon produced by carburization reaction is also changed at the same rate, whereby the ratio thereof is constant.
By forming an oxide film on a portion of a product by the present invention, a product in which the carburization depth differs in portions can be produced. In the easiest method, after a work is preliminary oxidized, the oxide film of portions that do not require the oxide film are removed by grinding or cutting. Partial carburization can be performed by this method more easily than by conventional methods such as a partial carburization using an anti-carburizer (disclosed in Japanese Unexamined Patent Application Publication No. 10-273771 and Japanese Unexamined Patent Application Publication No. 4-32527), a partial carburization using plating (disclosed in Japanese Unexamined Patent Application Publication No. 8-60335), a method for controlling a carburization depth by utilizing plastic deformation (disclosed in Japanese Unexamined Patent Application Publication No. 5-25610), and a method in which unnecessary portions are removed by grinding or cutting after high concentration carburization (disclosed in Japanese Unexamined Patent Application Publication No. 4-250927).
When such a gear wheel is carburized by conventional decompressed carburization, the edge portion thereof may be excessively carburized. However, if decompressed carburization is performed by forming an oxide film at flat portions and removing the oxide film at the edge portions, the above problem does not occur.
When a material is carburized by a step using the preliminary oxidation of the present invention so as to have a carbon concentration of not less than that at which carbides are produced, for example, C=at least 0.8%, and it is maintained at a precipitation temperature of carbides, a structure in which carbides are precipitated can be obtained. For example, when SCM420H is used, the above structure can be obtained by heat treatment using a heating pattern shown in
Wear resistance and surface fatigue strength can be improved by precipitating carbides, but such high concentration carburization performed by conventional production methods takes time. On the other hand, a certain structure can be easily obtained by using the method of the present invention. For example, after forming an oxide film on a surface of a tooth and removing the oxide film at the bottom of the tooth, the root of the tooth, or the bottom and the root of the tooth according to the method of partial carburization described above, the tooth is carburized by using the heating pattern shown in
Increasing of carbon concentration by the step using the preliminary oxidation of the present invention improves austenite stability, and the amount of the austenite after quenching is controllable and can be increased.
Number | Date | Country | Kind |
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2007-077349 | Mar 2007 | JP | national |