KR100315358B1 - A serial type of gas carburization furnace - Google Patents
A serial type of gas carburization furnace Download PDFInfo
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- KR100315358B1 KR100315358B1 KR1019990048042A KR19990048042A KR100315358B1 KR 100315358 B1 KR100315358 B1 KR 100315358B1 KR 1019990048042 A KR1019990048042 A KR 1019990048042A KR 19990048042 A KR19990048042 A KR 19990048042A KR 100315358 B1 KR100315358 B1 KR 100315358B1
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- gas
- air
- discharge
- chamber
- product
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- 238000005255 carburizing Methods 0.000 claims abstract description 38
- 238000002347 injection Methods 0.000 claims abstract description 15
- 239000007924 injection Substances 0.000 claims abstract description 15
- 238000007599 discharging Methods 0.000 claims abstract description 7
- 230000002000 scavenging effect Effects 0.000 claims abstract description 3
- 238000005245 sintering Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 2
- 238000010791 quenching Methods 0.000 abstract description 7
- 230000000171 quenching effect Effects 0.000 abstract description 6
- 230000015556 catabolic process Effects 0.000 abstract description 3
- 238000006731 degradation reaction Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 39
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 229910052799 carbon Inorganic materials 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 239000010410 layer Substances 0.000 description 6
- 229910000831 Steel Inorganic materials 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000010348 incorporation Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 238000005275 alloying Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910000734 martensite Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C8/06—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
- C23C8/08—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases only one element being applied
- C23C8/20—Carburising
- C23C8/22—Carburising of ferrous surfaces
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
- C21D1/06—Surface hardening
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D2211/00—Microstructure comprising significant phases
- C21D2211/008—Martensite
Abstract
본 발명은 제품의 표면에 입계산화층의 발생을 최소화하여, 제품의 품질 및 내구성 저하를 방지할 수 있는 연속식 가스 침탄 장치에 관한 것이고, 본 발명에 따른 연속식 가스 침탄 장치는 반입실 내의 공기를 배출하도록 불활성 및 RX 가스를 주입하는 제 1 불활성 및 RX 가스 주입관과, 반입실로의 불활성 및 RX 가스의 주입에 따른 공기를 배출하기 위하여 반입실과 소통하는 제 1 공기 배출관과, 침탄된 제품을 소입조로 반출하기 위하여 침탄 영역과 소입조 사이에 위치되는 반출실과, 반출실 내의 공기를 배출하도록 불활성 및 RX 가스를 주입하는 제 2 불활성 및 RX 가스 주입관과, 반출실로의 불활성 및 RX 가스의 주입에 따른 공기를 배출하기 위하여 반출실에 연결되는 제 2 공기 배출관을 포함한다.The present invention relates to a continuous gas carburizing device capable of minimizing generation of grain boundary oxide layers on a surface of a product and preventing degradation of product quality and durability, and the continuous gas carburizing device according to the present invention provides air in a carrying room. First inert and RX gas inlet tubes for injecting inert and RX gas to discharge, first air outlet tubes communicating with the inlet chamber for discharging air following inertness into the loading chamber and injection of RX gas, and quenching the carburized product A discharge chamber located between the carburizing zone and the scavenging tank for carrying out into the tank, a second inert and RX gas injection tube for injecting inert and RX gas to discharge air in the discharge chamber, and inert and RX gas injection into the discharge chamber. And a second air discharge pipe connected to the discharge chamber to discharge the air accordingly.
Description
본 발명은 연속식 가스 침탄로에 관한 것이고, 보다 상세하게는 침탄로의 입구 도어와 출구 도어에 공기 혼입 방지용 챔버 및 공기 혼입 방지 시스템을 가지는 연속식 가스 침탄로에 관한 것이다.The present invention relates to a continuous gas carburizing furnace, and more particularly to a continuous gas carburizing furnace having an air mixing prevention chamber and an air mixing prevention system in the inlet and outlet doors of the carburizing furnace.
일반적으로, 침탄은 강재의 탄소함유량을 증가시키기 위하여 탄소를 강의 표면층에 침입·고용시키는 방법이며, 탄소농도가 낮은 연철의 표면부를 탄소농도가 높은 마르텐사이트로 변환하는 것을 목적으로 한 표면 경화법이며, 침탄된 강은 기어와 같이 잘 마모되지 않고 잘 갈라지지 않는 부품에 이용되고 있다. 침탄 후에 담금질을 하면 표면은 더욱 단단해지고 내마모성이 좋아진다. 또 중심부는 강인하여 충격저항이 높으므로 베어링, 피스톤링, 기계부품의 활주 부분 등에 가공된다. 침탄으로는 고체 침탄법·액체 침탄법·가스 침탄법이 있다.Generally, carburization is a method of infiltrating and employing carbon into the surface layer of steel in order to increase the carbon content of steel, and is a surface hardening method for converting the surface portion of soft iron having a low carbon concentration to martensite having a high carbon concentration. For example, carburized steel is used for hard-to-wear and hard-to-part parts such as gears. Quenching after carburizing makes the surface harder and wear-resistant. In addition, since the center part is strong and has high impact resistance, it is machined in bearings, piston rings, and sliding parts of mechanical parts. Carburizing includes solid carburizing, liquid carburizing and gas carburizing.
도 1에는 종래의 연속식 가스 침탄 장치가 도시되어 있으며, 연속식 가스 침탄 장치는 반입실(101), 예열 영역(102), 침탄 영역(103), 확산 영역(104), 강온 영역(105), 균열 영역(106) 및 소입조(107)를 포함한다.FIG. 1 shows a conventional continuous gas carburizing apparatus, and the continuous gas carburizing apparatus includes a loading chamber 101, a preheating region 102, a carburizing region 103, a diffusion region 104, and a temperature lowering region 105. , Crack region 106 and quenching tank 107.
반입실(101)을 소위 입구 챔버로서, 반입실(101)의 도어(108)가 개방되면, 침탄될 재료가 적재된 트레이가 반입실(101) 내로 반입된다. 반입실(101) 내로 반입된 트레이는 반입실(101)과 예열 영역(102)의 소통을 개폐하는 내부 도어(109)의 개방으로 예열 영역(102)으로 이송되고, 그런 다음 내부 도어(109)는 폐쇄된다.When the carrying room 101 is a so-called inlet chamber and the door 108 of the carrying room 101 is opened, the tray on which the material to be carburized is loaded is carried into the carrying room 101. The tray brought into the carrying room 101 is transferred to the preheating area 102 by the opening of the inner door 109 which opens and closes the communication between the carrying room 101 and the preheating area 102, and then the inner door 109. Is closed.
침탄될 재료는 예열 영역(102)에서 대략 800℃ 내지 900℃의 온도로 가열되고, 그런 다음, 침탄 영역(103)으로 이송된다. 침탄될 재료는 침탄 영역(103)에서도 상기된 바와 같은 온도로 유지된 상태에서, 제품의 표면에 탄소(C)가 침투되도록 침탄 처리된다. 침탄 영역(103)에서 침탄 처리된 재료는 확장 영역(104)으로 이송되어, 제품의 표면에 탄소가 침투된 제품은 확장 영역(104)을 통과하는 동안 제품의 내부까지 탄소가 확장되도록 처리된다.The material to be carburized is heated to a temperature of approximately 800 ° C. to 900 ° C. in the preheating region 102 and then transferred to the carburizing region 103. The material to be carburized is carburized so that carbon (C) penetrates into the surface of the product while the carburizing region 103 is maintained at the temperature as described above. The carburized material in the carburized region 103 is transferred to the expanded region 104 so that the product in which carbon has penetrated the surface of the product is treated to expand the carbon to the inside of the product while passing through the expanded region 104.
내부까지 탄소가 확장된 제품은 도어(110)의 개방으로 강온 영역(105)으로 이송되며, 강온 영역(105)에서 제품은 소입되도록 소정의 온도로 냉각되어, 도어(111)의 개방으로 균열 영역(106)으로 이송되어, 온도 분포가 균일하게 유지됨으로써, 제품의 품질이 균일하게 될 수 있다. 일정하게 균열이 완료된 제품은 도어(112)의 개방에 따라서 밖으로 반출되어, 소입조(107)로 이송된 후, 소입조(107)에서 소입된다.The product whose carbon is expanded to the inside is transferred to the temperature lowering region 105 by the opening of the door 110, and the product is cooled to a predetermined temperature to quench the product at the temperature lowering region 105, and thus the cracking region by the opening of the door 111. Transferred to 106, the temperature distribution is kept uniform, whereby the quality of the product can be made uniform. The product whose cracking is completed regularly is carried out with the opening of the door 112, is transferred to the sintering tank 107, and then quenched in the sintering tank 107.
그러나, 상기된 바와 같은 구조를 가지는 종래의 연속식 가스 침탄 장치는 반입실로부터 예열 영역으로 침탄될 재료가 이송될 때, 반입실의 내부에 혼입되어 있던 공기가 예열 영역으로 혼입됨으로써, 예열, 침탄 및 확산 영역의 분위기 가스가 분안정하게 되는 한편, 제품이 균열 영역으로부터 반출될 때, 도어(112)의 개방으로 인하여 공기가 균열 영역으로 혼입되어, 장치 내부의 분위기 상태가 불안정하게 될 수 있다.However, in the conventional continuous gas carburizing apparatus having the structure as described above, when the material to be carburized from the loading chamber is transferred to the preheating region, air mixed in the interior of the loading chamber is mixed into the preheating region, thereby preheating and carburizing. And the atmosphere gas in the diffusion region becomes stable, while when the product is taken out from the crack region, air may enter the crack region due to the opening of the door 112, resulting in an unstable atmosphere state inside the apparatus.
장치 내부로의 공기의 혼입은 산소량의 증가에 따라서 금속 표면의 합금 원소(Mn, Si, Cr 등)와 결합하여 산화되어 이로 인해 금속 조직 사이에서, 제품의 표면에 제품의 내구성 및 품질을 저하시키는 입계산화층의 형성을 촉진시키며, 분위기 가스 내에 산소(O2)가 많으면 입계산화층이 깊고 크게 발생된다. 이러한 입계산화층은 장치 내부의 분위기 가스 상태에 의해 좌우된다.The incorporation of air into the device combines with and oxidizes alloying elements (Mn, Si, Cr, etc.) on the metal surface as the amount of oxygen increases, thereby reducing the durability and quality of the product on the surface of the product, between the metal structures. The formation of the grain boundary oxide layer is promoted, and when the oxygen (O 2 ) is large in the atmosphere gas, the grain boundary oxide layer is deep and large. This grain boundary oxide layer is dependent on the atmospheric gas state inside the apparatus.
따라서, 본 발명의 목적은 제품의 표면에 입계산화층의 발생을 최소화하여,제품의 품질 및 내구성 저하를 방지할 수 있는 연속식 가스 침탄 장치를 제공하는데 있다.Accordingly, an object of the present invention is to provide a continuous gas carburizing apparatus that can minimize the generation of grain boundary oxide layer on the surface of the product, and can prevent degradation of the quality and durability of the product.
도 1은 종래의 연속식 가스 침탄 장치의 구조를 개략적으로 도시한 도면.1 is a view schematically showing the structure of a conventional continuous gas carburizing device.
도 2는 본 발명에 따른 연속식 가스 침탄 장치를 개략적으로 도시한 도면.Figure 2 schematically shows a continuous gas carburizing device according to the present invention.
(도면의 주요 부분에 대한 부호의 설명)(Explanation of symbols for the main parts of the drawing)
1 : 연속식 가스 침탄 장치 2 : 반입실1: continuous gas carburizing device 2: carrying room
3 : 제 1 불활성 및 RX 가스 주입관 4 : 제 1 공기 배출관3: first inert and RX gas injection pipe 4: first air discharge pipe
5, : 14 체크 밸브 6, 7, 15 : 도어5 ,: 14 check valve 6, 7, 15: door
8 : 예열 영역 9 : 소입조8: preheating area 9: hardening tank
10 : 침탄 영역 11 : 반출실10: carburizing area 11: unloading room
12 : 제 2 불활성 및 RX 가스 주입관 13 : 제 2 공기 배출관12 second inert and RX gas inlet tube 13 second air outlet tube
16 : 밸브16: valve
상기된 바와 같은 목적은, 제품이 반입되는 반입실, 반입실로부터 이송된 제품을 소정을 온도로 예열하여, 제품을 침탄하고 균일하게 가열하는 침탄 영역, 및 침탄된 제품을 소입하는 소입조를 포함하는 연속식 가스 침탄 장치에 있어서, 상기 반입실 내의 공기를 배출하도록 불활성 및 RX 가스를 주입하는 제 1 불활성 및 RX 가스 주입관과; 상기 반입실로의 불활성 및 RX 가스의 주입에 따른 공기를 배출하기 위하여 상기 반입실과 소통하는 제 1 공기 배출관과; 침탄된 제품을 소입조로 반출하기 위하여 침탄 영역과 소입조 사이에 위치되는 반출실과; 상기 반출실 내의 공기를 배출하도록 불활성 및 RX 가스를 주입하는 제 2 불활성 및 RX 가스 주입관과; 상기 반출실로의 불활성 및 RX 가스의 주입에 따른 공기를 배출하기 위하여 상기 반출실에 연결되는 제 2 공기 배출관을 포함하는 것을 특징으로 하는 본 발명에 따른 연속식 가스 침탄 장치에 의하여 달성된다.The object as described above includes an entry chamber into which a product is brought in, a carburizing zone for preheating a product transferred from the carrying room to a temperature, carburizing and uniformly heating the product, and a quenching tank for quenching the carburized product. A continuous gas carburizing apparatus comprising: a first inert and RX gas inlet tube for injecting inert and RX gas to discharge air in the carrying-in chamber; A first air discharge pipe communicating with the carrying room for discharging air due to the inertness into the carrying room and the injection of RX gas; A discharge chamber located between the carburizing zone and the scavenging tank to take out the carburized product into the sintering tank; A second inert and RX gas injection tube for injecting inert and RX gas to discharge air in the discharge chamber; It is achieved by the continuous gas carburizing apparatus according to the invention, characterized in that it comprises a second air discharge pipe connected to the discharge chamber for discharging the air according to the inert to the discharge chamber and the injection of RX gas.
상기에서, 상기 제 1 및 제 2 공기 배출관은 바람직하게 외부로부터 상기 반입실 및 상기 반출실로 공기의 혼입을 방지하기 위하여 체크 밸브가 각각 설치된다.In the above, the first and second air discharge pipes are preferably provided with check valves, respectively, to prevent the mixing of air from the outside into the carrying-in chamber and the carrying-out chamber.
이하, 본 발명의 바람직한 실시예를 명세서에 첨부된 도면을 참조하여 보다 상세하게 설명한다.Hereinafter, preferred embodiments of the present invention will be described in more detail with reference to the accompanying drawings.
도 2는 본 발명에 따른 연속식 가스 침탄 장치를 개략적으로 도시한 도면이다. 도 2에 도시된 바와 같이, 본 발명에 따른 연속식 가스 침탄 장치(1)는 반입실(2) 내의 공기를 배출하도록 반입실(2) 내로 불활성 및 RX 가스를 주입하는 제 1 불활성 및 RX 가스 주입관(3)이 반입실(2)에 연결된다. 불활성 및 RX 가스가 제 1 불활성 및 RX 가스 주입관(3)을 통하여 반입실(2)로 주입됨으로써, 반입실(2) 내의 공기가 외부로 배출된다.2 is a view schematically showing a continuous gas carburizing apparatus according to the present invention. As shown in FIG. 2, the continuous gas carburizing apparatus 1 according to the present invention is a first inert and RX gas which injects inert and RX gas into the loading chamber 2 to discharge air in the loading chamber 2. The injection tube 3 is connected to the carrying room 2. Inert and RX gas is injected into the carrying-in chamber 2 through the 1st inert and RX gas injection pipe 3, and the air in the carrying-in chamber 2 is discharged | emitted to the outside.
제 1 공기 배출관(4)은 반입실(2) 내로 불활성 및 RX 가스의 주입에 의하여 반입실(2) 내의 공기를 외부로 배출하기 위하여 반입실(2)에 연결되며, 바람직하게 외부로부터 반입실(2)로 공기의 혼입을 방지하기 위하여 체크 밸브(5)가 설치된다.The first air discharge pipe 4 is connected to the loading chamber 2 for discharging the air in the loading chamber 2 to the outside by inert and RX gas injection into the loading chamber 2, preferably from the outside. A check valve 5 is provided to prevent the mixing of air into (2).
따라서, 반입실(2)의 도어(6)가 개방되면, 침탄될 재료가 적재된 트레이가 반입실(2) 내로 반입된 후에, 상기된 바와 같이 불활성 및 RX 가스가 제 1 불활성 및 RX 가스 주입관(3)을 통하여 반입실(2)로 주입됨으로써, 반입실(2) 내의 공기가 제 1 공기 배출관(4)을 통하여 외부로 배출된다. 반입실(2)로부터 공기가 완전히 배출되면, 도어(7)가 개방되고, 트레이는 침탄될 재료가 종래의 기술에서 설명된 바와 같은 침탄 처리가 행해진도록 예열 영역(8)으로 이송된다.Therefore, when the door 6 of the loading chamber 2 is opened, after the tray on which the material to be carburized is loaded is loaded into the loading chamber 2, the inert and RX gas is injected into the first inert and RX gas as described above. By injecting into the carrying-in chamber 2 through the pipe 3, the air in the carrying-in chamber 2 is discharged | emitted through the 1st air discharge pipe 4 to the outside. When the air is completely discharged from the carrying-in chamber 2, the door 7 is opened and the tray is transferred to the preheating region 8 so that the carburized material is subjected to the carburizing treatment as described in the prior art.
침탄 처리된 제품은 침탄 영역(10)과 소입조(9)사이에 위치되는 반출실(11)로 이송되며, 반출실(11) 또한 반출실(11) 내의 공기를 배출하도록 불활성 및 RX 가스를 주입하는 제 2 불활성 및 RX 가스 주입관(12) 및 반출실(11)로의 불활성 및 RX 가스의 주입에 따른 공기를 배출하기 위한 제 2 공기 배출관(13)이 제공된다. 제 2 공기 배출관(13) 또한 외부로부터 반출실(11)로 공기의 혼입을 방지하기 위하여 체크 밸브(14)가 설치된다.The carburized product is transferred to the discharge chamber 11 located between the carburizing zone 10 and the quenching tank 9, and the discharge chamber 11 also discharges inert and RX gas to discharge the air in the discharge chamber 11. A second inert and RX gas inlet tube 12 for injecting and a second air outlet tube 13 for discharging air according to the inertness into the discharge chamber 11 and the injection of the RX gas are provided. The second air discharge pipe 13 is also provided with a check valve 14 to prevent mixing of air into the discharge chamber 11 from the outside.
이러한 구성을 가지는 것에 의하여, 제품이 반출실(11)로 이송되면, 도어(15)가 개방되면서, 제품이 소입조(9)로 이송되며 소입되며, 이 때, 반출실(11)로 혼입된 공기는 상기된 바와 같은 과정을 통하여 외부로 배출된다. 그러므로, 다음의 제품 트레이가 침탄 영역으로 장입되어도, 침탄 영역은 일정한 가스 분위기를 유지하므로, 공기의 혼입으로 인한 제품 표면에서의 입계산화층의 유발이 방지된다.By having such a configuration, when the product is transported to the carrying out chamber 11, the door 15 is opened, and the product is transferred to the sintering tank 9 and quenched, and at this time, the product is mixed into the carrying out chamber 11 Air is discharged to the outside through the process as described above. Therefore, even if the next product tray is charged into the carburized region, the carburized region maintains a constant gas atmosphere, thereby preventing the induction of grain boundary layer on the product surface due to the incorporation of air.
한편, 제 1 및 제 2 불활성 및 RX 가스 주입관(3,12)에는 불활성 및 RX 가스를 반입실(2) 및 반출실(11)에 공급 및 차단하기 위한 밸브(16)가 각각 설치된다.The first and second inert and RX gas injection pipes 3 and 12 are provided with valves 16 for supplying and blocking the inert and RX gas to the loading chamber 2 and the discharge chamber 11, respectively.
상기된 바와 같은 구조를 가지는 본 발명에 따른 연속식 가스 침탄 장치에 의하면, 제품의 반입 및 반출시에, 침탄 영역으로의 공기의 혼입이 방지됨으로써, 공기의 혼입으로 인한 제품의 표면에 입계산화층의 발생을 최소화하여, 제품의 품질 및 내구성 저하를 방지할 수 있다.According to the continuous gas carburizing apparatus according to the present invention having the structure as described above, when the product is loaded and unloaded, the mixing of air into the carburized region is prevented, thereby providing the grain boundary layer on the surface of the product due to the mixing of air. By minimizing the occurrence, it is possible to prevent degradation of product quality and durability.
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