[0001] The present invention relates to a method for gas carburizing steel parts used, for
example, in the automobile industry or machine industry.
[0002] When gas carburizing of steel treatment objects is carried out, the carburizing treatment
time can be shortened by raising the carburizing temperature. However, if the carburizing
temperature becomes too high, the treatment object melts down. For this reason, the
carburizing temperature that has been conventionally used in practice was less than
the eutectic point temperature (in the case of an iron-carbon equilibrium diagram
shown in Fig. 1, it is the C point temperature which is 1147°C) at which the liquid
phase is transformed into γ iron and cementite, and usually was not higher than 1050°C.
[0003] In order to shorten the carburizing treatment time at the conventional carburizing
temperature, the carburizing treatment was carried out till the concentration of carbon
in the surface layer of the treatment object became higher than the final target value,
and then diffusion treatment which caused the carbon in the surface layer of the treatment
object to diffuse was carried out in a high-temperature atmosphere with a carbon concentration
less than that of the carburizing atmosphere, thereby decreasing the carbon concentration
in the surface layer to the final target value (Japanese Examined Patent Publication
No.
1994-45868). However, when the carburizing temperature is limited to a temperature less than
the eutectic point temperature, the diffusion rate of carbon atoms in the treatment
object is restricted. Therefore, the carburizing time cannot be shortened significantly.
Thus, the problem is that the diffusion treatment requires a long time, thereby reducing
productivity.
[0004] It is an object of the present invention to provide a method of gas carburizing capable
of resolving the aforesaid conventional problems.
[0005] A method of gas carburizing according to an aspect of the present invention comprises
the steps of predetermining limiting carburizing conditions at which the surface layer
of a sample of a steel treatment object present in a carburizing atmosphere is austenitized
without melting at a carburizing temperature which is not higher than a peritectic
point temperature at which δ iron and liquid phase are transformed into γ iron and
not less than a eutectic point temperature at which liquid phase is transformed into
γ iron and cementite; and gas carburizing the treatment object under carburizing conditions
which are set so as not to contradict the limiting carburizing conditions, at a carburizing
temperature which is not higher than the peritectic point temperature and not less
than the eutectic point temperature, wherein the limiting carburizing conditions comprise
an upper limit value of a partial pressure of carburizing gas in the carburizing atmosphere
at which the surface layer of the sample is austenitized without melting. Thus, the
carburizing time is shortened by gas carburizing the treatment object which is austenitized
by being heated to a highest possible temperature. By increasing the carburizing gas
concentration in the carburizing atmosphere, the hardened layer of the treatment object
can be prevented from becoming shallow and have sufficient thickness within a short
time.
The treatment object is austenitized when heated to a temperature above the GS line
or ES line in the iron-carbon equilibrium diagram shown in Fig. 1. If the concentration
of carbon in the surface layer of the treatment object exceeds the JE line, melting
is started in the surface layer. The present inventor has found out that an upper
limit value of a partial pressure of carburizing gas at which the surface layer of
the treatment object is not melted exists under given carburizing conditions such
as carburizing temperature and carburizing time, and that this upper limit value decreases
with the increase in carburizing temperature and increases with the decrease in carburizing
time. Because the carburizing temperature range in the method of gas carburizing in
accordance with the present invention is from not higher than the peritectic point
temperature (1494°C) to not less than the eutectic point temperature (1147°C), the
carburizing time can be greatly reduced. Moreover, setting the partial pressure of
carburizing gas to not higher than the predetermined upper limit value makes it possible
to carry out carburizing at a high temperature without causing melting in the surface
layer of the treatment object. As a result, the amount of consumed energy can be greatly
reduced and energy can be saved. Furthermore, the gas carburizing process can be carried
out in series with other processes, for example, machining processes or different
heat treatment processes.
[0006] It is preferred that the limiting carburizing conditions comprise an upper limit
value of carburizing temperature and an upper limit value of carburizing time at which
the surface layer of the sample is austenitized without melting, the relationship
between the upper limit value of the partial pressure of carburizing gas, the upper
limit value of carburizing temperature, and the upper limit value of carburizing time
is predetermined, and the partial pressure of carburizing gas, carburizing temperature,
and carburizing time are set such that the carburizing conditions of the treatment
object do not contradict the limiting carburizing conditions which satisfy the predetermined
relationship. The upper limit value of the partial pressure of carburizing gas, the
upper limit value of carburizing temperature, and the upper limit value of carburizing
time serving as the limiting carburizing conditions are interrelated and one of the
upper limit values can be found by fixing the other two conditions among the partial
pressure of carburizing gas, carburizing temperature, and carburizing time. As a result,
the conditions providing for the fastest possible carburization can be easily set
within a range in which the surface layer of the treatment object is not melted.
[0007] A method of gas carburizing according to another aspect of the present invention
is characterized in that when gas carburization of a steel treatment object is carried
out, a carburizing temperature is set at a temperature which is not higher than a
peritectic point temperature (it is the J point temperature which is 1494°C in the
case shown in Fig. 1) at which δ iron and liquid phase are transformed into γ iron
and not less than a eutectic point temperature (it is the C point temperature which
is 1147°C in the case shown in Fig. 1) at which liquid phase is transformed into γ
iron and cementite, a target value of carbon concentration in the surface of the treatment
object is set at a value which is not higher than a value at which the surface of
the treatment object is not melted at the set carburizing temperature, and a partial
pressure of carburizing gas in the carburizing atmosphere is set at a value at which
the carbon concentration in the surface of the treatment object can reach the set
target value as a result of gas carburization carried out during a preset time. The
present invention is based on the discovery that when the carburizing temperature
is set at a temperature which is not higher than the peritectic point temperature
and is not less than the eutectic point temperature and the target value of carbon
concentration in the surface of the steel treatment object is set at a value which
is not higher than the value at which the surface of the treatment object is not melted
at the set carburizing temperature, if the partial pressure of carburizing gas in
the carburizing atmosphere is set at an appropriate value, then the carbon concentration
in the surface of the treatment object can reach the set target value as a result
of gas carburization and a sufficient carburizing depth can be obtained. Because carburization
at a high temperature increases the movement rate of carbon atoms in the course of
carburization over that attained by the conventional technology, the hardened layer
depth that required several hours to be attained by the conventional technology can
be attained within a short time. Moreover an excess increase in the concentration
of carbon in the surface is prevented.
As a result, the carburizing time can be shortened significantly by raising the carburizing
temperature. Moreover, because the concentration of carbon in the surface layer of
the treatment object does not exceed the set target value, the carbon diffusion treatment
process is unnecessary. As a result, productivity can be increased. Furthermore, the
gas carburizing treatment process can be carried out in series with other heat treatment
processes. Therefore, it is preferred that the treatment object is cooled without
carrying out a diffusion treatment after the gas carburization has been carried out.
It is also preferred that the treatment object is reheated after the cooling. The
reheating is carried out, for example, by induction heating. It is also preferred
that quenching treatment of the reheated treatment object is carried out. Cooling
for the quenching treatment is carried out, for example, by oil cooling or gas cooling.
In terms of shortening the carburizing time, it is preferred that the carburizing
temperature is set at 1200°C or higher.
In this case, prior to implementing the method of gas carburizing, it is preferred
that limiting carburizing conditions are predetermined, those conditions are set such
that the surface layer of a sample of a steel treatment object present in a carburizing
atmosphere is austenitized without melting at a carburizing temperature which is not
higher than the peritectic point temperature at which δ iron and liquid phase are
transformed into γ iron and is not less than the eutectic point temperature at which
liquid phase is transformed into γ iron and cementite. The limiting carburizing conditions
comprise the upper limit value of the partial pressure of carburizing gas in the carburizing
atmosphere at which the surface layer of the sample is austenitized without melting.
The treatment object is austenitized when heated to a temperature above the GS line
or ES line in the iron-carbon equilibrium diagram shown in Fig. 1. If the concentration
of carbon in the surface layer of the treatment object exceeds the JE line, melting
is started in the surface layer. An upper limit value of the partial pressure of carburizing
gas at which the surface layer of the treatment object is not melted exists under
given carburizing conditions such as carburizing temperature and carburizing time.
Predetermining the limiting carburizing conditions comprising the upper limit value
of the partial pressure of carburizing gas facilitates setting the partial pressure
of carburizing gas and carburizing time.
[0008] In the present invention, the total pressure of carburizing atmosphere can be a normal
pressure, or can be decreased or increased with respect to the normal pressure. The
entire carburizing atmosphere can be a carburizing gas, or a gas mixture of a carburizing
gas and a dilute gas can be used as the carburizing atmosphere. When a dilute gas
is used, dilution is preferably carried out with an inert gas such as nitrogen gas
or argon gas. No specific limitation is placed on the type of steel of the treatment
object which is subjected to gas carburizing by the method according to the present
invention, and the method of the present invention is applicable to any steel provided
that it can be austenitized at a temperature which is not higher than the peritectic
point temperature and not less than the eutectic point temperature. This steel can
be not only a carbon steel but also an alloy steel.
[0009] In the present invention, it is preferred that heating of the treatment object and
a sample thereof is carried out with means capable of high-speed heating of the surface
layer thereof. The heating is preferably carried out, for example, by induction heating
or laser heating. As a result, heating efficiency of the carburization object can
be increased. Furthermore, because the carburizing treatment is simplified, quality
control is facilitated. Thus, because the number of factors affecting the quality
is small, even if quality problems such as spots, strains, or cracks in the treatment
object are encountered, the causes thereof can be easily clarified. Furthermore, a
wall covering the carburizing treatment space can be a cold wall and a waste gas combustion
apparatus is unnecessary; therefore, degradation of working conditions is prevented
and initial investment is reduced, moreover the method is applicable to single-item
and small-scale production and can be easily incorporated into a production line,
for example, in-line treatment of the individual production can be carried out. Because
the conventional carburizing treatment furnace equipped with thermally insulating
walls is not required, furnace heating or seasoning become unnecessary and running
cost can be reduced.
[0010] In the present invention, the gas carburizing is preferably carried out, while causing
a carburizing atmosphere comprising the carburizing gas at a constant partial pressure
to flow. As a result, a constant partial pressure of carburizing gas can be maintained
and treated products of uniform quality can be obtained.
[0011] The method of gas carburizing according to the present invention can greatly improve
productivity.
Brief Description of Drawings
[0012]
Fig. 1 is an iron-carbon equilibrium diagram.
Fig. 2 illustrates the state of heating a sample of the treatment object by the gas
carburizing apparatus in an embodiment of the present invention.
Fig. 3 illustrates an example of relationship between the upper limit value of partial
pressure of carburizing gas, different carburizing temperatures and carburizing times.
Fig. 4 illustrates the state of heating a treatment object with the gas carburizing
apparatus in an embodiment of the present invention.
Fig. 5 illustrates the relationship between the carburizing treatment time till the
surface of the treatment object starts melting at a carburizing temperature of 1573
K, partial pressure of carburizing gas, and concentration of carbon in the surface.
Fig. 6 illustrates the relationship between the carburizing treatment time till the
surface of the treatment object starts melting at a carburizing temperature of 1623
K, partial pressure of carburizing gas, and concentration of carbon in the surface.
Fig. 7 shows the relationship between the hardness and the distance (depth) from the
surface of the treatment object carburized with a carburizing time of 1 min at a carburizing
temperature of 1250°C in an example of the present invention.
Fig. 8 shows the relationship between the hardness and the distance (depth) from the
surface of the treatment object carburized with a carburizing time of 1 min at a carburizing
temperature of 1300°C in an example of the present invention.
Fig. 9 shows the relationship between the hardness and the distance (depth) from the
surface of the treatment object carburized with a carburizing time of 10 min at a
carburizing temperature of 1250°C in an example of the present invention.
Fig. 10 shows the relationship between the hardness and the distance (depth) from
the surface of the treatment object carburized with a carburizing time of 10 min at
a carburizing temperature of 1300°C in an example of the present invention.
Fig. 11 is a microphotograph as a substitution for a drawing illustrating the metallurgical
structure prior to quenching in the surface layer of the gas-carburized treatment
object.
Fig. 12 is a microphotograph as a substitution for a drawing illustrating the metallurgical
structure after quenching in the surface layer of the gas-carburized treatment object.
Fig. 13 illustrates the relationship between the concentration of carbon and the distance
(depth) from the surface of the treatment object obtained in an example of the present
invention.
Fig. 14 illustrates an example of the relationship between the carburizing time, diffusion
time, and concentration of carbon in the treatment object that was treated by the
conventional carburizing method.
[0013] The gas carburizing apparatus for performing the method of the present invention
shown in Fig. 2 comprises a vacuum container 1, a heating device 2, a vacuum pump
3 for reducing the pressure inside the vacuum container 1, and a gas source 4 for
supplying gas for carburizing atmosphere into the vacuum container 1. In the present
embodiment, the heating device 2 carries out induction heating inside the vacuum container
1 with a coil 2a connected to a power source 7. The output of the power source 7 to
the coil 2a is variable.
[0014] First, in order to carry out gas carburization of a sample 5' of a steel treatment
object, a thermocouple 6 is welded as a sensor for temperature detection to the surface
layer of the sample 5' set in the heating device 2. Then, the pressure inside the
vacuum container 1 is reduced by evacuating the vacuum container 1 with the vacuum
pump 3. At this time, the pressure inside the vacuum container 1 is preferably about
27 Pa or less. Means for detecting the temperature is not limited to a thermocouple.
[0015] After such pressure reduction, a gas for carburizing atmosphere is introduced from
the gas source 4 into the vacuum container 1. As a result, the vacuum container 1
is filled with the carburizing atmosphere and the total pressure of the carburizing
atmosphere is raised. For example, the pressure of the carburizing atmosphere inside
the vacuum container 1 is raised to about 80 kPa. The carburizing atmosphere is composed
of a carburizing gas and a dilute gas. No specific limitation is placed on the type
of the carburizing gas or dilute gas. The carburizing gas of the present embodiment
is methane gas and the dilute gas is nitrogen gas. Using a hydrocarbon gas as the
carburizing gas makes it possible to realize a non-oxidizing carburization. The carburizing
gas is not limited to hydrocarbon gases. The carburizing atmosphere may also be composed
only of a carburizing gas.
[0016] In order to maintain a constant total pressure of carburizing atmosphere inside the
vacuum container 1, the gas for carburizing atmosphere is supplied from the gas source
4 into the vacuum container 1 at a constant flow rate, and the gas for carburizing
atmosphere is released by the vacuum pump 3 at a constant flow rate. As a result,
the gas for carburizing atmosphere flows inside the vacuum container 1 at a constant
flow rate of, for example, 0.5 L/min, and the total pressure of the carburizing atmosphere
is maintained at, for example, about 80 kPa. Thus, the carburizing atmosphere containing
a carburizing gas at a constant partial pressure flows inside the vacuum container
1. The partial pressure of carburizing gas is a value obtained by multiplying the
total pressure of carburizing atmosphere inside the vacuum container 1 by a molar
fraction or volume percent of the carburizing gas. Therefore, the set value of the
partial pressure of carburizing gas can be adjusted by changing the total pressure
of carburizing atmosphere inside the vacuum container 1 or by changing the flow rate
ratio of the carburizing gas and dilute gas.
[0017] Then, the sample 5' is heated with the heating device 2 to a set carburizing temperature.
The carburizing temperature is not higher than the peritectic point temperature at
which δ iron and liquid phase are transformed into γ iron and not less than the eutectic
point temperature at which liquid phase is transformed into γ iron and cementite.
The set value of the carburizing temperature can be adjusted by changing the output
of the heating device 2 to the coil 2a.
[0018] When the sample 5' is gas carburized by holding for the set carburizing time under
the set partial pressure of carburizing gas and the set carburizing temperature, it
is checked to see whether the surface layer of the sample 5' is melted or not.
[0019] If the surface layer of the sample 5' has not melted during the carburization, another
carburization of another sample 5' is carried out by increasing the set value of the
partial pressure of carburizing gas. If the surface layer of the sample 5' has melted,
another carburization of another sample 5' is carried out by decreasing the set value
of the partial pressure of carburizing gas. By repeating this process, the upper limit
value of the partial pressure of carburizing gas is predetermined as a limit carburizing
condition at which austenitization is conducted without melting the surface layer
of the sample 5'.
[0020] A method for predetermining the upper limit value of the partial pressure of carburizing
gas by fixing the carburizing temperature and carburizing time was described hereinabove,
but this method can be appropriately modified without departing from the essence of
the present invention. Thus, the upper limit value of carburizing time can be found
by fixing the partial pressure of carburizing gas and carburizing temperature, or
the upper limit value of carburizing temperature can be found by fixing the partial
pressure of carburizing gas and carburizing time.
[0021] Fig. 3 shows an example of the relationship between the upper limit value of the
partial pressure of carburizing gas, the upper limit value of carburizing temperature,
and the upper limit value of carburizing time predetermined in the above-described
manner. In the present embodiment, the concentration of methane (vol%) in carburizing
atmosphere corresponding to the partial pressure of carburizing gas is plotted on
the ordinate in Fig. 3, but the partial pressure of carburizing gas may also be represented
by another. For example, when no dilute gas is used, the partial pressure of carburizing
gas is equal to the total pressure of carburizing atmosphere, and therefore the methane
flow rate can be used to represent the partial pressure of carburizing gas. By using
a similar method it is possible to find not only the lines for 1 min, 3 min, and 30
min shown in Fig. 3, but also any line or curve located therebetween. As shown in
Fig. 3, the upper limit value of the partial pressure of carburizing gas in the carburizing
atmosphere decreases with the increase in carburizing temperature and increases with
the decrease in carburizing time. Further, the relationship shown in Fig. 3 is merely
an example, and this relationship differs depending on the arrangement of structural
components of heating device 2, material and arrangement of sample 5' to the heating
device 2, type of heating device 2, type and flow rate of carburizing gas, and the
like.
[0022] Gas carburization of a steel treatment object 5 is thereafter carried out by using
the above-described apparatus for gas carburization under the carburizing conditions
which are set so as not to contradict the limiting carburizing conditions satisfying
the predetermined relationship. Carburization of the steel treatment object 5 can
be carried out in the same manner as carburization of the sample 5'.
[0023] To be more precise, as shown in Fig. 4, the steel treatment object 5 is set to the
heating device 2, the air present inside the vacuum container 1 is evacuated with
the vacuum pump 3, a gas for carburizing atmosphere is introduced into the vacuum
container 1 from the gas source 4 to raise the pressure of the carburizing atmosphere
to the set pressure, the gas for carburizing atmosphere is supplied at a constant
flow rate from the gas source 4 into the vacuum container 1, and the gas for carburizing
atmosphere is released at a constant flow rate with the vacuum pump 3. As a result,
the partial pressure of carburizing gas in the carburizing atmosphere inside the vacuum
container 1 is set at not higher than the upper limit value that was predetermined
as a limiting carburization condition. Then, the steel treatment object 5 is heated
to the carburizing temperature with the heating device 2. The carburizing temperature
is set at a value which is not higher than the aforesaid peritectic point temperature
and not less than the eutectic point temperature. The carburizing temperature during
heating of the sample 5' can be reproduced during heating of the treatment object
5 by controlling the heating device 2 in the same manner as during heating of the
sample 5', and therefore, it is not necessary to weld the thermocouple 6 to the treatment
object 5. Gas carburization is carried out by holding the treatment object 5 for the
set carburizing time under the set partial pressure of carburizing gas and set carburizing
temperature.
[0024] For example, when gas carburization of the steel treatment object 5 is carried out,
the carburizing temperature is set at a temperature which is not higher than the peritectic
point temperature at which δ iron and liquid phase are transformed into γ iron and
not less than the eutectic point temperature at which liquid phase is transformed
into γ iron and cementite. Furthermore, the target value of carbon concentration in
the surface of the treatment object 5 is set at a value which is not higher than a
value at which the surface of the treatment object 5 is not melted at the set carburizing
temperature. Further, the partial pressure of carburizing gas in the carburizing atmosphere
is set at a value at which the carbon concentration in the surface of the treatment
object can reach the set target value as a result of gas carburization carried out
during a preset period. The set value of the partial pressure of carburizing gas corresponding
to the carburizing time can be predetermined by experiments. The set values of the
carburizing time and partial pressure of carburizing gas are less than the aforesaid
upper limit values corresponding to the set temperature. Therefore, the setting of
the carburizing time and partial pressure of carburizing gas is facilitated by predetermining
the aforesaid upper limit values.
For example, because the surface of the treatment object 5 starts melting at a carbon
concentration of about 1.15 wt.% at a carburizing temperature of 1573 K, the relationship
between the carburizing treatment time required for the surface of the treatment object
5 to start melting at a carburizing temperature of 1573 K, the partial pressure of
carburizing gas, and the concentration of carbon in the surface is expressed by Fig.
5 from the relationship shown in Fig. 3. Fig. 5 demonstrates that when the carburizing
temperature is set at 1573 K and the target value of carbon concentration in the surface
of treatment object 5 is set at a concentration of less than 1.15 wt.% at which no
melting occurs, the concentration of methane in the carbon atmosphere should be set
at less than 10 vol% if the carburizing time is 1 min, and the concentration of methane
in the carbon atmosphere should be set at less than 3 vol% if the carburizing time
is 10 min. Furthermore, for example, since the surface of the treatment object 5 starts
melting at a carbon concentration of about 0.9 wt.% at a carburizing temperature of
1623 K, the relationship between the carburizing treatment time required for the surface
of the treatment object 5 to start melting at the carburizing temperature of 1623
K, the partial pressure of carburizing gas, and the concentration of carbon in the
surface is shown by Fig. 6 from the relationship shown in Fig. 3. Fig. 6 demonstrates
that when the carburizing temperature is set at 1623 K and the target value of carbon
concentration in the surface of steel treatment object 5 is set at a concentration
of less than 0.9 wt.% at which no melting occurs, the concentration of methane in
the carbon atmosphere should be set at less than 1.8 vol% if the carburizing time
is 1 min, and the concentration of methane in the carbon atmosphere should be set
at less than 0.8 vol% if the carburizing time is 10 min.
[0025] Gas carburizing is carried out by holding the treatment object 5 for a set carburizing
time under the aforesaid set partial pressure of carburizing gas and set carburizing
temperature. Once the set carburizing time has elapsed, the carburizing is stopped
by stopping the supply of carburizing gas or terminating the heating with the heating
device 2.
[0026] With the method of gas carburizing according to the present invention, the carburizing
time can be greatly shortened because the carburizing temperature range is set between
not higher than the peritectic point temperature and not less than the eutectic temperature.
Moreover, setting the partial pressure of carburizing gas to not higher than the predetermined
upper limit value makes it possible to carry out the carburization at a high temperature
without melting the surface layer of the steel treatment object 5. For example, the
diffusion coefficient of carbon atoms in γ iron is 3.59 x 10
-5 mm
2/sec at a temperature of 1000°C, but increases to ten or more times, that is, 43 x
10
-5 mm
2/sec at a temperature of 1300°C. Thus, the migration speed of carbon atoms at a temperature
of 1300°C is not less than tenfold that at a temperature of 1000°C. Therefore, the
time required to obtain the desired carburization depth can be greatly reduced and
the usual carburization depth can be obtained at a carburizing time of about 1 to
10 min. Moreover, because the concentration of carbon in the surface layer of the
treatment object 5 does not exceed the set target value, a carbon diffusion treatment
step becomes unnecessary. As a result, the carburizing treatment time can be greatly
shortened and the productivity can be increased. Furthermore, the gas carburization
treatment step can be carried out in series with other heat treatment steps. Setting
the carburizing temperature at not less than 1200°C is preferred from the standpoint
of shortening the carburizing time, and this temperature can be set at not less than
1300°. Furthermore, because gas carburization is carried out while causing the carburizing
atmosphere comprising the carburizing gas at a constant partial pressure to flow inside
the vacuum container 1, a constant partial pressure of carburizing gas can be maintained
and the uniformity of the quality of treatment object 5 can be improved. Moreover,
no soot generation was observed in the carburizing treatment implemented according
to the present invention, and in this respect, too, the present invention is greatly
superior to the conventional vacuum carburizing.
[0027] Once the aforesaid gas carburizing has been completed, the treatment object 5 is
cooled without carrying out the diffusion treatment. No specific limitation is placed
on the cooling method, and natural cooling or a variety of forced cooling methods
can be used. Furthermore, the treatment object 5 subjected to gas carburization is
preferably quenched by reheating after cooling and then rapidly cooling. A secondary
quenching may also be carried out by employing the primary cooling as a rapid cooling.
The atmosphere for carrying out the quenching is preferably a neutral protective atmosphere,
that is, the atmosphere in which the treatment object is neither carburized nor decarburized
at this temperature, but the treatment can be carried out in another atmosphere of
such as inert gas. The reheating temperature for quenching is set at not less than
the temperature at which at least the surface layer of the treatment object 5 is austenitized
above the GS line or ES line in the equilibrium diagram shown in Fig. 1.
Example 1
[0028] With the method of gas carburizing of the above-described embodiment according to
the present invention, the limiting carburizing conditions were predetermined and
gas carburization was carried out under the carburizing conditions that are set so
as not to contradict the limiting carburizing conditions. The treatment object 5 had
a shape of right cylinder with a diameter of 10 mm and a length of 52 mm made of a
aickel-chromium-molybdenum steel (Japanese Industrial Standard SNCM420). In the present
example, the carburized treatment object 5 was naturally cooled inside the vacuum
container 1, hardened, polished, and finish processed with a diamond paste with a
particle size of 3 micrometers, followed by hardness measurements and structure observations.
The vacuum container 1 was purged prior to the carburization. The carburizing gas
was methane and the dilute gas was nitrogen. During carburization, the gas for carburizing
atmosphere was caused to flow inside the vacuum container 1 at a constant flow rate
of 0.5 L/min. Hardening was carried out by holding the treatment object 5 for 10 min
inside a quartz tube furnace kept at a temperature of 860°C in which the nitrogen
gas atmosphere was flowed and then quenched into oil. It goes without saying that
furnaces of other types, including the induction heating furnaces, can be used for
the hardening.
Fig. 7 shows the relationship between the hardness (Hv) and the distance (depth) (mm)
from the surface of the treatment object 5 that was gas carburized under the following
carburizing conditions: carburizing temperature 1250°C, carburizing time 1 min, and
concentration corresponding to partial pressure of methane, which is the carburizing
gas, 40 vol%. In this case, the target value of carbon concentration in the surface
of the treatment object 5 was set at 1.4 wt.%.
Fig. 8 shows the relationship between the hardness (Hv) and the distance (depth) (mm)
from the surface of the treatment object that was gas carburized under the following
carburizing conditions: carburizing temperature 1300°C, carburizing time 1 min, and
concentration of methane, which is the carburizing gas, 10 vol%. In this case, the
target value of carbon concentration in the surface of the treatment object 5 was
set at 1.15 wt.%.
Fig. 9 shows the relationship between the hardness (Hv) and the distance (depth) (mm)
from the surface of the treatment object 5 that was gas carburized under the following
carburizing conditions: carburizing temperature 1250°C, carburizing time 10 min, and
concentration corresponding to partial pressure of methane, which is the carburizing
gas, 10 vol%. In this case, the target value of carbon concentration in the surface
of the treatment object 5 was set at 1.4 wt.%.
Fig. 10 shows the relationship between the hardness (Hv) and the distance (depth)
(mm) from the surface of the treatment object that was gas carburized under the following
carburizing conditions: carburizing temperature 1300°C, carburizing time 10 min, and
concentration of methane, which is the carburizing gas, 3 vol%. In this case, the
target value of carbon concentration in the surface of the treatment object 5 was
set at 1. 15 wt.%.
Figs. 7 through 10 confirm that the carburized layer with a sufficient effective carburization
depth can be obtained within a carburizing time of 1 through 10 min. Further, the
partial pressure of methane, which is a carburizing gas, is obtained by multiplying
the total pressure of carburizing atmosphere by the methane concentration. In the
example shown in Figs. 7 through 10, the total pressure of carburizing atmosphere
was about 80 kPa.
The metal structure prior to quenching of the surface layer of the treatment object
5 subjected to gas carburizing at a carburizing temperature of 1300°C for a carburizing
time of 1 min in accordance with the present invention is shown in Fig. 11. The metallurgical
structure after quenching is shown in Fig. 12. A coarse structure that was present
prior to quenching is not present after the quenching, which confirms that quenching
makes the coarse structure fine.
Example 2
[0029] Gas carburization was carried out under the carburizing conditions that were set
by the gas carburization method of the above-described embodiment of the present invention.
The treatment object 5 had a shape of right cylinder with a diameter of 10 mm and
a length of 52 mm made of a nickel-chromium-molybdenum steel (Japanese Industrial
Standard SNCM420) as used in the above-described embodiment. The carburized treatment
object 5 was naturally cooled inside the vacuum container 1, without being subjected
to diffusion treatment, then was hardened, polished, and finish processed with a diamond
paste with a particle size of 3 micrometers. The vacuum container 1 was purged prior
to the carburization. The carburizing gas was methane and the dilute gas was nitrogen.
Hardening was carried out by holding the treatment object 5 for 10 min inside a quartz
tube furnace kept at a temperature of 860°C in which nitrogen gas atmosphere was flowed
and then quenched into oil. It goes without saying that furnaces of other types, including
the induction heating furnaces, can be used for the hardening. The carburizing temperature
was 1300°C, the carburizing time was 1 min, the concentration corresponding to the
partial pressure of methane, which is the carburizing gas, in the carburizing atmosphere
was 10 vol%, the target value of carbon concentration in the surface of the treatment
object 5 was 0.74 wt.%, the total pressure of carburizing atmosphere was 80 kPa, and
the gas for carburizing atmosphere was flowed inside the vacuum container 1 during
the carburization at a constant flow rate of 0.5 L/min. Fig. 13 shows the relationship
between the concentration of carbon (wt.%) and the distance (depth) (mm) from the
surface of the treatment object 5 obtained in the present example. In the present
example, the depth to which the concentration of carbon was higher than 0.2 wt.% of
the base metal, that is, the complete carburizing depth, was 0.9 mm, thereby confirming
that the sufficient effective carburizing depth can be obtained without employing
a diffusion treatment step. Furthermore, the results obtained were matched well with
the results on the complete carburizing depth obtained from Fig. 8.
[0030] According to the above-described examples, the concentration of carbon in the surface
of the treatment object 5 can be brought to the target value and a sufficient carburizing
depth can be obtained without employing a diffusion treatment. By contrast, Fig. 14
shows an example of the relationship between the concentration of carbon in the surface
and carburizing time in the treatment object obtained by the conventional carburizing
method, in which because the concentration of carbon exceeds the target value when
only the carburizing treatment is carried out, a subsequent diffusion treatment has
to be carried out.
[0031] The present invention makes it possible to shorten significantly the carburizing
time by raising the carburizing temperature. Moreover, because the concentration of
carbon in the surface layer of the treatment object 5 does not exceed the set target
value, the carbon diffusion treatment becomes unnecessary and productivity can be
increased.
1. A method of gas carburizing comprising the steps of:
predetermining limiting carburizing conditions at which a surface layer of a sample
of a steel treatment object present in a carburizing atmosphere is austenitized without
melting at a carburizing temperature which is not higher than a peritectic point temperature
at which a δ iron and liquid phase are transformed into γ iron and is not less than
a eutectic point temperature at which liquid phase is transformed into γ iron and
cementite; and
gas carburizing the treatment object under carburizing conditions which are set so
as not to contradict the limiting carburizing conditions, at a carburizing temperature
which is not higher than the peritectic point temperature and is not less than the
eutectic point temperature, wherein
the limiting carburizing conditions comprises:
an upper limit value of a partial pressure of carburizing gas in the carburizing atmosphere
at which the surface layer of the sample is austenitized without melting;
an upper limit value of carburizing temperature at which the surface layer of the
sample is austenitized without melting and an upper limit value of carburizing time
at which the surface layer of the sample is austenitized without melting;
a relationship between the upper limit value of the partial pressure of carburizing
gas, the upper limit value of carburizing temperature, and the upper limit value of
carburizing time is predetermined; and
a partial pressure of carburizing gas, a carburizing temperature and a carburizing
time are set as a set of carburizing conditions of the treatment object so as not
to contradict the limiting carburizing conditions which satisfy the predetermined
relationship.
2. The method of carburizing gas according to claim 1, wherein said upper limit value
of the partial pressure of carburizing gas, said upper limit of carburizing temperature,
said upper limit of carburizing temperature, and said upper limit of carburizing time
are determined by fixing two of said partial pressure of carburizing gas, said carburizing
temperature, or said carburizing time.
3. The method of carburizing gas according to claim 2, wherein said upper limit of said
partial pressure of carburizing gas is found by fixing the carburizing temperature
and the carburizing time.
4. The method of gas carburizing according to claim 1, wherein
a target value of carbon concentration in the surface of the treatment object is set
at a value which is not higher than a value at which the surface of the treatment
object is not melted at the set carburizing temperature; and
a partial pressure of carburizing gas in a carburizing atmosphere is set at a value
at which the carbon concentration in the surface of the treatment object can reach
the set target value as a result of gas carburization carried out during a preset
time.
5. The method of gas carburizing according to claim 4, wherein the treatment object is
cooled without carrying out a diffusion treatment after the gas carburization has
been carried out.
6. The method of gas carburizing according to claim 5, wherein the treatment object is
reheated after cooling.
7. The method of gas carburizing according to claim 6, wherein hardening of the reheated
treatment object is carried out.
8. The method of gas carburizing according to any of claims 4 to 7, wherein the carburizing
temperature is set at 1200°C or higher.
1. Gasaufkohlungsverfahren umfassend die Schritte:
Vorherbestimmung von limitierenden Aufkohlungsbedingungen, bei denen eine Oberflächenschicht
einer Probe eines zu behandelnden Gegenstandes aus Stahl, die in einer Aufkohlungsatmosphäre
vorhanden ist, ohne Schmelzen bei einer Aufkohlungstemperatur austenitisiert wird,
die nicht höher als die Temperatur eines peritektischen Punktes ist, bei der ein δ-Eisen
und flüssige Phase in γ-Eisen transformiert wird und nicht geringer als die Temperatur
des eutektischen Punktes ist, bei der eine flüssige Phase in γ-Eisen und Zementit
transformiert ist; und
Gasaufkohlung des zu behandelnden Gegenstandes unter Aufkohlungsbedingungen, die so
gesetzt sind, daß sie den limitierenden Aufkohlungsbedingungen nicht widersprechen,
bei einer Aufkohlungstemperatur, die nicht höher als die Temperatur des peritektischen
Punktes und nicht niedriger als die Temperatur des eutektischen Punktes ist, wobei
die limitierenden Aufkohlungsbedindungen umfassen:
einen oberen Grenzwert eines Partialdrucks des Aufkohlungsgases in der Aufkohlungsatmosphäre,
bei der die Oberflächenschicht der Probe ohne Schmelzen austenitisiert,
einen oberen Grenzwert einer Aufkohlungstemperatur, bei der die Oberflächenschicht
der Probe ohne Schmelzen austenitisiert und einen oberen Grenzwert der Aufkohlungszeit,
bei der die Oberflächenschicht der Probe ohne Schmelzen austenitisiert;
es wird eine Beziehung zwischen dem oberen Grenzwert des Partialdrucks des Aufkohlungsgases,
dem oberen Grenzwert der Aufkohlungstemperatur und dem oberen Grenzwert der Aufkohlungszeit
vorherbestimmt; und
es werden ein Partialdruck des Aufkohlungsgases, eine Aufkohlungstemperatur und eine
Aufkohlungszeit als ein Satz von Aufkohlungsbedingungen des zu behandelnden Gegenstandes
eingestellt, so daß sie nicht den limitierenden Aufkohlungsbedingungen widersprechen,
die die vorherbestimmte Beziehung erfüllen.
2. Gasaufkohlungsverfahren nach Anspruch 1, bei dem der obere Grenzwert des Partialdrucks
des Aufkohlungsgases, der obere Grenzwert der Aufkohlungstemperatur, der obere Grenzwert
der Aufkohlungstemperatur und der obere Grenzwert der Aufkohlungszeit durch Fixieren
von zweien der besagten Partialdrucke des Aufkohlungsgases, der Aufkohlungstemperatur
oder der Aufkohlungszeit bestimmt werden.
3. Gasaufkohlungsverfahren nach Anspruch 2, bei dem der obere Grenzwert des Partialdrucks
des Aufkohlungsgases durch Fixieren der Aufkohlungstemperatur und der Aufkohlungszeit
gefunden wird.
4. Gasaufkohlungsverfahren nach Anspruch 1, bei dem
ein Targetwert der Kohlenstoffkonzentration in der Oberfläche des Behandlungsobjekts
bei einem Wert eingestellt wird, der nicht höher als der Wert ist, bei dem die Oberfläche
des zu behandelnden Gegenstandes bei der eingestellten Aufkohlungstemperatur nicht
geschmolzen wird; und
ein Partialdruck des Aufkohlungsgases in der Aufkohlungsatmosphäre wird eingestellt
bei einem Wert, bei dem die Kohlenstoffkonzentration in der Oberfläche des zu behandelnden
Gegenstandes den gesetzten Targetwert als ein Ergebnis der Gasaufkohlung erreichen
kann, die während einer vorgegebenen Zeit durchgeführt wird.
5. Gasaufkohlungsverfahren nach Anspruch 4, bei dem der zu behandelnde Gegenstand ohne
Durchführung einer Diffusionsbehandlung gekühlt wird, nachdem die Gasaufkohlung durchgeführt
wurde.
6. Gasaufkohlungsverfahren nach Anspruch 5, bei dem der zu behandelnde Gegenstand nach
dem Kühlen wieder erhitzt wird.
7. Gasaufkohlungsverfahren nach Anspruch 6, bei dem ein Härten des wieder erhitzten zu
behandelnden Gegenstandes durchgeführt wird.
8. Gasaufkohlungsverfahren nach einem der Ansprüche 4 bis 7, bei dem die Aufkohlungstemperatur
auf 1200°C und höher eingestellt wird.
1. Un procédé de cémentation gazeuse, comprenant les étapes consistant à :
prédéterminer des conditions limites de cémentation auxquelles une couche superficielle
d'un échantillon d'un objet de traitement en acier présent dans une atmosphère carburante
est austénitisée sans fondre, à une température de cémentation qui n'est pas supérieure
à une température de point péritectique à laquelle un fer δ et une phase liquide sont
transformés en fer γ, et qui n'est pas inférieure à une température de point eutectique
à laquelle la phase liquide est transformée en fer γ et cémentite ; et
réaliser une cémentation gazeuse de l'objet de traitement dans des conditions de cémentation
qui sont fixées de manière à ne pas contredire les conditions limites de cémentation,
à une température de cémentation qui n'est pas supérieure à la température de point
péritectique et qui n'est pas inférieure à la température de point eutectique, dans
lequel
les conditions limites de cémentation comprennent :
une valeur limite supérieure d'une pression partielle de gaz de cémentation dans l'atmosphère
carburante à laquelle la couche superficielle de l'échantillon est austénitisée sans
fondre ;
une valeur limite supérieure de température de cémentation à laquelle la couche superficielle
de l'échantillon est austénitisée sans fondre et une valeur limite supérieure de temps
de cémentation à laquelle la couche superficielle de l'échantillon est austénitisée
sans fondre ;
une relation entre la valeur limite supérieure de la pression partielle de gaz de
cémentation, la valeur limite supérieure de température de cémentation et la valeur
limite supérieure de temps de cémentation est prédéterminée ; et
une pression partielle de gaz de cémentation, une température de cémentation et un
temps de cémentation sont fixés comme un ensemble de conditions de cémentation de
l'objet de traitement de manière à ne pas contredire les conditions limites de cémentation
qui satisfont la relation prédéterminée.
2. Procédé de cémentation gazeuse selon la revendication 1, dans lequel ladite valeur
limite supérieure de la pression partielle de gaz de cémentation, ladite limite supérieure
de température de cémentation, ladite limite supérieure de température de cémentation,
et ladite limite supérieure de temps de cémentation sont déterminées en fixant deux
parmi ladite pression partielle de gaz de cémentation, ladite température de cémentation
et ledit temps de cémentation.
3. Procédé de cémentation gazeuse selon la revendication 2, dans lequel ladite limite
supérieure de ladite pression partielle de gaz de cémentation est découverte en fixant
la température de cémentation et le temps de cémentation.
4. Procédé de cémentation gazeuse selon la revendication 1, dans lequel
une valeur cible de concentration de carbone dans la surface de l'objet de traitement
est fixée à une valeur qui n'est pas supérieure à une valeur à laquelle la surface
de l'objet de traitement n'est pas fondue à la température de cémentation fixée ;
et
une pression partielle de gaz de cémentation dans une atmosphère carburante est fixée
à une valeur à laquelle la concentration de carbone dans la surface de l'objet de
traitement peut atteindre la valeur cible fixée du fait de la cémentation gazeuse
réalisée pendant une durée prédéfinie.
5. Procédé de cémentation gazeuse selon la revendication 4, dans lequel l'objet de traitement
est refroidi sans réaliser un traitement de diffusion après réalisation de la cémentation
gazeuse.
6. Procédé de cémentation gazeuse selon la revendication 5, dans lequel l'objet de traitement
est réchauffé après le refroidissement.
7. Procédé de cémentation gazeuse selon la revendication 6, dans lequel le durcissement
de l'objet de traitement réchauffé est réalisé.
8. Procédé de cémentation gazeuse selon l'une quelconque des revendications 4 à 7, dans
lequel la température de cémentation est fixée à 1200° C. ou plus.