Gas-carburizing process

Abstract: A gas-carburizing process wherein an article is treated by feeding a hydrocarbon gas and an oxidative gas of raw material gases directly into an atmospheric heat treating furnace, characterized in that, when the pressure within the furnace is negative, CO₂ is fed in as a negative pressure dissolving means. A gas-carburizing apparatus wherein a gas inlet for feeding a hydrocarbon gas and an oxidative gas provided in the ceiling part of an atmospheric heat treating furnace is provided with a CO₂ feeding part for dissolving the negative pressure within the furnace.

Description: This invention relates to a gas-carburizing process hardening the surface of a steel part by diffusing carbon into the surface layer of the steel part. In a general gas carburizing process, not only an atmospheric heat treating furnace (called a heat treating furnace hereinafter) but also a transforming furnace has been conventionally required. Such a transforming furnace, necessary to obtain a transformed gas for the atmospheric heat treatment, is charged with a catalyst and is fed with a hydrocarbon gas and air in a retort heated from outside. The gas obtained from the above mentioned transforming furnace is fed to the above mentioned heat treating furnace and a carburizing gas is added to the gas to adjust the carbon potential of the atmospheric gas within the heat treating furnace. However, with the above mentioned conventional process, there have remained such problems as, not only a heat treating furnace but also a transforming furnace is required, heat energy and an expensive catalyst are required and further it is expensive to maintain and control the heater and retort. Therefore, in consideration of the uneconomy accompanying the use of the above mentioned transforming furnace, the applicant of the present case has provided a process for feeding a hydrocarbon gas and oxidative gas directly into a heat treating furnace without using a transforming furnace (Japanese Patent Publication No.38870/1989). In this process, a hydrocarbon gas and a small amount of pure oxygen are introduced into a heat treating furnace kept above 730°C and nitrogen gas is excluded to carry out a carburizing process. That is to say, when a hydrocarbon gas and pure oxygen are introduced into a heat treating furnace kept at a predetermined temperature, an atmosphere necessary for carburization will be produced to carry out carburization. According to this process, as only the gas contributing directly to carburization is fed into the heat treating furnace, the apparent partial pressure of CO in the atmosphere will not be reduced by the gas not contributing directly to the carburization, and therefore the carburizing efficiency is high. Furthermore no transforming furnace is required, the used amount of the hydrocarbon gas is small and the process is very economical. However, in the above mentioned process, the amount of gas fed into the furnace is so much smaller than in the case of the process using the carburizing gas transformed in the above mentioned transforming furnace that, with the opening and closing of an inlet door, intermediate door or outlet door when an article to be treated is put in or removed, the pressure within the furnace becomes negative, atmospheric air (oxygen) will be sucked in through the packing part of the door and the atmosphere within the furnace will be disturbed to cause a danger of an explosion or the like. Therefore, the applicant of the present application has provided an atmospheric furnace pressure adjusting apparatus wherein, when the pressure within the furnace is negative, a ring burner provided in an atmospheric air introducing path is ignited to feed the combustion gas into the furnace to dissolve the negative pressure within the furnace (Japanese Utility Model Application Publication No.16766/1989). If this apparatus is used, when the pressure within the furnace is negative, oxygen will not be introduced and the furnace will be safe but the N 2 gas not directly contributing to the above mentioned carburization will be introduced thereby reducing the partial pressure of CO within the furnace. The basic gas reaction of the carburization is as follows: CO CO 2 = K H 2 H 2 O 2CO → [ C ] + CO 2 That is to say, the gas contributing directly to the carburization is CO, the larger the partial pressure of CO, the more active the carburization, and a carburized layer of a required hardness and depth can be formed within a shortertime. Furthermore the dispersion of the carburization of a treated article of a complicated form can be reduced and a pore or the like can be effectively carburized. This invention as defined in claim 1 provides a more economic gas-carburizing process wherein, as mentioned above, when the pressure within a heat treating furnace is negative, the N 2 gas or the like not contributing directly to the carburization will be prevented from being introduced so that the partial pressure of CO in the atmosphere may not be reduced and the quality of the treated article may be improved. That is to say, in the process of the invention,when the pressure within a heat treating furnace is negative (i.e. below atmospheric pressure) CO 2 will be fed in so that the negative pressure within the furnace may be counteracted and the partial pressure of CO in the atmosphere may be increased. Without using a transforming furnace, a hydrocarbon gas and oxidative gas are fed directly into a heat treating furnace and, when the pressure within the heat treating furnace is below atmospheric pressure, CO 2 is fed in quickly. Preferred embodiments of the invention are described below with reference to the accompanying drawings in which: Fig. 1 is a vertically sectioned view of a batch type heat treating furnace; Fig. 2 is a vertically sectioned view of a continuous type heat treating furnace; Fig. 3 is a partly sectioned magnified elevation of a gas inlet; and Fig. 4 is a graph showing the relation between the cycle time and carburization depth. A batch furnace is shown in Fig. 1 in which the reference numeral 1 represents a heating chamber, 2 represents a cooling chamber (quenching chamber), 3 represents an inlet door of the heating chamber 1, 3a represents an opening and closing port provided in the inlet door 3, 4 represents an intermediate door, 4a represents an outflow port provided in the intermediate door 4, 5 represents an outlet door of the cooling chamber 2, 6 represents a cooling oil, 7 represents a furnace pressure adjusting apparatus of the above mentioned atmospheric furnace, 8 represents a curtain flame ignited when the outlet door 5 is opened, 9 represents an agitating fan which is supported in the ceiling part by a fan shaft 10 and is rotated by a motor (not illustrated) provided outside and 11 represents a gas inlet provided in the ceiling part adjacent to the above mentioned agitating fan 10 to feed in a hydrocarbon gas and oxidative gas. In the same drawing, the reference numeral 12 represents a hydrocarbon gas feeding port, 13 represents an oxidative gas feeding port, 15 represents a hydrocarbon gas source, 16 represents an opening and closing valve controlling the fed amount of the above mentioned hydrocarbon gas, 17 represents an oxidative gas source and 18 represents an opening and closing valve controlling the fed amount of the above mentioned oxidative gas. In the carburizing apparatus used in the present invention, a CO 2 feeding part is formed in the above mentioned gas inlet 11. A CO 2 feeding port 14 is formed at the end outside the furnace of the above mentioned gas inlet 11 and a CO 2 source 19 is connected to the above mentioned CO 2 feeding port through an opening and closing valve 20 controlling the fed amount of CO 2 . If the apparatus is formed so that the high pressure CO 2 may be fed as required from the feeding port 14, the soot deposited in the above mentioned gas inlet 11 as detailed later can be removed without disturbing the atmosphere within the furnace. Also, the reference numeral 21 represents a CO 2 feeding path to the cooling chamber 2 and 22 represents an opening and closing valve controlling the fed amount of the above mentioned CO 2 . In the above mentioned formation, when the inlet door 3 of the heating chamber 1 is opened, an article to be treated is put into the heating chamber 1 and the inlet door 3 is closed, much air will-have entered the heating chamber 1. Needless to say, the temperature within the heating chamber 1 is so high that O 2 in the air will be perfectly consumed by the combustion with the hydrocarbon and N 2 gas will remain. Therefore, in the present invention, the opening and closing valve 20 is opened, CO 2 is fed into the heating chamber 1 and, at the same time, the opening and closing port 3a provided in the inlet door 3 is opened to discharge the N 2 gas within the heating chamber out of the furnace. The opening and closing port 3a is provided in the above mentioned inlet door 3 in order to elevate the efficiency of discharging the N 2 gas within the heating chamber 1, because, in case the above mentioned opening and closing port 3a is not provided, the N 2 gas within the heating chamber 1 will enter the cooling chamber 2 through the outflow port 4a or the like of the intermediate door 4, will push up the opening and closing valve (not illustrated) of the furnace pressure adjusting apparatus 7 of the above mentioned atmosphere and will be discharged out of the furnace. However, in fact, a large amount of the N 2 gas will remain within the cooling chamber 2, will further leak through the packing part of the intermediate door 4 and will be circulated within the heating chamber 1 in some case. Therefore, the opening and closing port 3a is lower in resistance than the outflow port 4a of the intermediate door 4 and larger than the outflow port 4a so that the N 2 gas may be preferably discharged through the above mentioned opening and closing port 3a. Also, the feed of the above mentioned CO 2 is to prevent a negative pressure phenomemon from being temporarily produced in case an article to be treated is put at the normal temperature into the heating chamber 1 and the inlet door 3 is closed. Then, in quenching the article being treated, in case the intermediate door 4 is opened and the article is transferred to the cooling chamber, the air within the cooling chamber 2 will be expanded by the radiation heat of the heating chamber 1 and the heated article but, when the intermediate door 4 is closed, the radiation heat from the heating chamber 1 will be interrupted and, when the article is then dipped into the cooling oil, the pressure in the cooling chamber 2 will become negative. In order to dissolve this negative pressure, the opening and closing valve 22 is opened and CO 2 is fed to the cooling chamber 2 to prevent the negative pressure phenomenon. Then, the outlet door 5 is opened, the curtain flame 8 is ignited and the treated article is carried out of the furnace. When the outlet door 5 is closed and the curtain flame 8 is extinguished, the pressure within the cooling chamber 2 will become negative again and atmospheric air will be sucked in through the above mentioned furnace pressure adjusting apparatus 7 of the atmosphere, the outlet door 5 part and the like to be likely to cause an explosion. Therefore, the opening and closing valve 22 is opened again and CO 2 is fed to the cooling chamber 2 to dissolve the negative pressure. It has been confirmed that the CO within the furnace can be maintained substantially at about 40% in the above mentioned operation. That is to say, CO in % in the atmosphere in the present invention is as follows in the calculation: Needless to say, in the actual operation, the above mentioned calculated values will be reduced by the entry of air through the door packing part, the entry of air at the time of the negative pressure caused by the furnace operation and the like. For example, in the case of the above mentioned formula (3), CO in % in the actual operation was about 40%. Also, CO in % in the calculation of the invention mentioned in the above mentioned Japanese Patent Application Publication No.38870/1989 was as follows: Needless to say, CO in % in the actual operation was about 30%. Further, in case air is added instead of pure oxygen, CO in % in the calculation is as follows: As mentioned above, according to the present invention, as different from the respective conventional processes, CO in the atmosphere is prevented as much as possible from being thinned, the carburizing capacity is not reduced, a carburized layer of a required hardness and depth can be formed within a shortertime and the process is economical. A continuous furnace is shown in Fig. 2 in which the same parts as in Fig. 1 bear the same reference numerals. In Fig. 2, the reference numeral 23 represents a carry-in chamber and 24 represents a carry-in door. In this embodiment, after completion of the carburization, a continuous operation will set in and then when the carry-in door 24, inlet door 3, intermediate door 4 and outlet door 5 are closed, respective negative pressure phenomena will be produced. . Needless to say, if the inlet door 3 and intermediate door 4 are opened simultaneously whilst closing the carry-in door 24, one of the above mentioned negative pressure phenomena can be reduced. Also, as the furnace is continuous, even if CO 2 is fed to any of the carry-in chamber 23, heating chamber 1 and cooling chamber 5, the negative pressure can be dissolved. Therefore, in the embodiment shown in the drawing, the carry-in chamber 23 is provided with a CO 2 feeding path 25 and an opening and closing valve 26 controlling the fed amount of CO 2 . Also, in the embodiment of this continuous furnace, the same as in the embodiment of the above mentioned batch furnace, CO 2 was fed to the cooling chamber 2 and the process was observed. However, it has been confirmed that, if CO 2 is fed to the cooling chamber 2, the grain field oxidation will increase and it is not proper. In this embodiment, the case of opening the opening and closing valve 26 and feeding in CO 2 is when the inlet door 3 and intermediate door 4 are closed and when the outlet door 5 is closed, except in the above mentioned case. Also, in this embodiment, only the hydrocarbon gas is made to flow in the heating chamber 1 and the oxidative gas has been confirmed to be sufficient with only the CO 2 purging gas of the carry-in chamber. In Fig. 4 is shown a relation between the cycle time and carburized depth in the case that, without using a transforming furnace (gas), a hydrocarbon gas and an oxidative gas were fed directly into a furnace to carburize a gear and in the case that the same gear was treated by a conventional process. In the graph in Fig. 4, the lines (a) and (b) represent the process of the present invention, that is, the case of treating with: (Example 1) Enriched gas (CH 4 ) 30ℓ /min. CO 2 3ℓ /min. CO 2 purging gas 300ℓ /min. The line (a) shows the state of the tooth surface part and the line (b) shows the state of the tooth bottom part. The lines (c) and (d) represent treatment for the same time as in the above mentioned present invention with a conventional process, that is, (Example 2) Enriched gas (CH 4 ) 30ℓ /min. Air 3ℓ /min. The line (c) shows the state of the tooth surface part and the line (d) shows the state of the tooth bottom part. As mentioned above, according to the process of the present invention, if the time is the same, a deeper carburized depth can be obtained and, in the case of obtaining the same carburized depth, the time can be shortened. It shall be described in the following to remove soot deposited within the above mentioned gas inlet 11. In the gas-carburizing process of the above mentioned present invention, that is, if a hydrocarbon gas and an oxidative gas are mixed within the gas inlet 11 and are fed into the furnace, they will incompletely pyrolize in a sooting temperature region before they reach the furnace at a high temperature, and will be deposited as soot 27 within the gas inlet 11 as shown in Fig. 3 thereby narrowing the gas feeding path within the gas inlet 11 and powder particles will drop onto the upper surface of the article to be treated to generate a foul product in some cases. As a method of removing the above mentioned soot 27, an oxidative gas is fed into the gas inlet 11 to burn out the soot 27 or high pressure air is fed to forcibly remove the soot 27. However, in either method, the partial pressure of CO within the furnace will be reduced and the quality of the treated article will be reduced. However, in the apparatus used in the present invention, if high pressure CO 2 is fed from the CO 2 feeding port 14 as synchronized with opening the inlet door 3 or carry-in door 24 in putting in the article to be treated, the above mentioned soot 27 deposited within the gas inlet 11 will be able to be removed and the partial pressure of CO will not be reduced. The above mentioned high pressure CO 2 may be fed when the deposition of the soot 27 within the gas inlet 11 is confirmed or periodically. That is to say, in the case of the batch furnace shown in Fig. 1, the high pressure CO 2 may be fed in by opening the opening and closing valve 20 in conformity with opening the inlet door 3. In the case of the continuous furnace in Fig. 2, as the gas inlets 11 are provided at proper intervals in the heating chamber 1, the above mentioned soot 27 will be removed sequentially. That is to say, first of all, in the first cycle, high pressure CO 2 is fed to the gas inlet 11 nearest to the carry-in chamber 23 to remove the soot 27, then, in the next cycle, high pressure CO 2 is fed to the second gas inlet 11 to remove the soot 27 and sequentially the soot 27 of the gas inlet 11 is removed so that the deposition of the soot 27 within the gas inlet 11 may be prevented and the generation of a foul product of the treated article may be prevented.

Claims: A gas-carburizing process comprising treating an article with a hydrocarbon gas and an oxidative gas which are fed directly into a heat treating furnace, characterised in that said furnace is operated at atmospheric pressure and that CO 2 gas is fed in whenever the pressure within the furnace falls below atmospheric pressure, thereby increasing the partial pressure of CO within the furnace. A process as claimed in claim 1 wherein said article is a steel part. A process as claimed in claim 1 or claim 2 wherein said oxidative gas is pure oxygen. A process as claimed in any one of claims 1 to 3 wherein said atmospheric heat treating furnace is a batch or continuous furnace. A process as claimed in any one of claims 1 to 4 wherein deposited soot is removed from within the gas inlet by the incoming CO 2 .

Inventors: ABUKAWA FUMITAKA, GOI HITOSHI, KITAYAMA YOSHIHIKO, NANBA KEISHICHI, WATANABA MASAHIKO, ABUKAWA, FUMITAKA, GOI, HITOSHI, KITAYAMA, YOSHIHIKO, NANBA, KEISHICHI, WATANABA, MASAHIKO, Abukawa, Fumitaka, c/o Tokyo Heat Treating Co Ltd, Goi, Hitoshi, c/o Tokyo Heat Treating Co. Ltd,, Nanba, Keishichi, c/o Tokyo Heat Treating Co Ltd, Watanaba, Masahiko, c/o Tokyo Heat Treating Co Ltd
Applicants: DOWA MINING CO, MITSUBISHI MOTORS CORP, DOWA MINING CO., LTD., MITSUBISHI JIDOSHA KOGYO KABUSHIKI KAISHA
Application year: 1991
Main classification: C23C8
IPC codes: C23C8