KR980009473A - Refining method of low carbon, low nitrogen stainless steel - Google Patents
Refining method of low carbon, low nitrogen stainless steel Download PDFInfo
- Publication number
- KR980009473A KR980009473A KR1019960031002A KR19960031002A KR980009473A KR 980009473 A KR980009473 A KR 980009473A KR 1019960031002 A KR1019960031002 A KR 1019960031002A KR 19960031002 A KR19960031002 A KR 19960031002A KR 980009473 A KR980009473 A KR 980009473A
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- carbon
- stainless steel
- nitrogen
- concentration
- low
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
- C21C7/068—Decarburising
- C21C7/0685—Decarburising of stainless steel
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/005—Manufacture of stainless steel
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D3/00—Charging; Discharging; Manipulation of charge
- F27D3/16—Introducing a fluid jet or current into the charge
- F27D2003/162—Introducing a fluid jet or current into the charge the fluid being an oxidant or a fuel
- F27D2003/163—Introducing a fluid jet or current into the charge the fluid being an oxidant or a fuel the fluid being an oxidant
- F27D2003/164—Oxygen
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D3/00—Charging; Discharging; Manipulation of charge
- F27D3/16—Introducing a fluid jet or current into the charge
- F27D2003/168—Introducing a fluid jet or current into the charge through a lance
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Treatment Of Steel In Its Molten State (AREA)
Abstract
본 발명은 저탄소, 저질소 스텐인레스강의 정련방법에 대한 것으로, 정련로에 장입되는 스테인레스용강의 탄소농도를 1.8%-2.0중량%로 조절하고, 정련로의 탈탄과정에서 탄소를 제거하기 위해 공급하는 산소의 취입방법으로, 1.8-2.0중량%의 탄소농도에서 0.7-0.8중량%까지는 상취랜스(lance)를 이용하고, 그 이하의 탄소농도에서는 상취랜스를 사용하지 않고 횡취 투이어(tuyere)만을 이용하여 산소를 취입하는 것으로 이루어지며, 이로써 스테인레스강의 탄소농도 저감에 문제를 야기시키지 않으면서 질소농도를 낮출 수 있으며, 이 결과 연속 주조시 TiN에 의한 침적노즐의 막힘현상을 현저하게 개선하는 효과가 얻어진다.The present invention relates to a method for refining low-carbon and low-nitrogen stainless steel, wherein the carbon concentration of the stainless steel molten steel charged into the refining furnace is adjusted to 1.8% to 2.0% by weight, A lancing lance is used at a carbon concentration of 1.8-2.0 wt% up to 0.7-0.8 wt%, and a lance is used at a carbon concentration of 1.8-2.0 wt%, using only a transversal tuyere Thereby reducing the nitrogen concentration without causing a problem in reducing the carbon concentration of the stainless steel. As a result, the clogging phenomenon of the deposition nozzle by the TiN during continuous casting is remarkably improved .
Description
본 발명은 저탄소, 저질소의 Ti 안정화 스테인레스강의 제조시 AOD 정련로에서의 질소농도를 낮추는 정련방법에 관한 것이다.The present invention relates to a refining method for lowering the nitrogen concentration in an AOD refining furnace in the production of low-carbon and low-quality Ti-stabilized stainless steels.
스테인레스강중의 탄소, 질소는 가공중의 연신율 및 용접부의 인성 저하등 철강제품의 여러 가지 기계적 성질을 나쁘게 하기 때문에 해로운 원소로 알려져 있다. 스테인레스강은 크롬, 망간등 탄소 및 질소와의 친화력이 높은 원소를 다량 함유하고 있기 때문에 스테인레스강의 정련시에 탄소 및 질소를 제거하는 기술은 매우 중요하다. 특히 STS409L강과 같이 Ti를 함유하는 강은 탄소 및 질소가 각각 탄화물 또는 질화물을 형성하기 때문에 두 성분의 농도를 낯추어야 하는데 특히 질소의 경우에는 응고 과정중에TiN이 생성되어 연속주조시의 노즐 막힘현상을 일으키거나 열연 코일의 표면 결함을 야기시키므로 용강중의 질소농도를 적극적으로 감소시켜야 한다.Carbon and nitrogen in stainless steels are known as harmful elements because they degrade various mechanical properties of steel products such as elongation during processing and decrease in toughness of welded parts. Since stainless steel contains a large amount of elements with high affinity for carbon and nitrogen, such as chromium and manganese, it is very important to remove carbon and nitrogen during refining of stainless steel. In particular, the steel containing Ti, such as STS409L steel, has to be different in the concentration of the two components because carbon and nitrogen form carbide or nitride, respectively. Especially, in case of nitrogen, TiN is formed during the solidification process, Or causing surface defects of the hot-rolled coil, the nitrogen concentration in the molten steel must be actively reduced.
제1도는 11.5% Cr을 함유한 스테인레스강에서 온도에 따른 용강중 [Ti]와 [N] 관계를 나타낸 것으로 Ti농도가 증가함에 따라 용해 질소농도가 감소하는 것을 볼 수 있다. 만일 용강중 질소가 용해질소 농도보다 높으면 질소는 TiN이 되어 석출하게 되며 TiN은 전술한 바 같은 제반 문제를 야기시키게 된다. 또한 도면으로부터 동일 Ti농도에서 용강온도가 감소할수록 용해 질소농도도 감소한다. 즉, 정련로 용강 출강후 주조할때까지 용강의 온도는 점차 감소하게 되는데, 이에 따라 고온에서 용해된 질소가 TiN으로 석출하게 되므로 STS409L의 질소농도는 STS409L의 응고온도(1505℃)에서의 질소농도(0.15%Ti에서 약 100ppm)보다 낮추어 주는 것이 바람직하다.Figure 1 shows the relationship between [Ti] and [N] in molten steel with temperature in 11.5% Cr-containing stainless steels. It can be seen that the concentration of dissolved nitrogen decreases with increasing Ti concentration. If nitrogen in the molten steel is higher than the dissolved nitrogen concentration, nitrogen becomes TiN and precipitates, and TiN causes all of the problems described above. Also, as the molten steel temperature decreases at the same Ti concentration, the nitrogen concentration also decreases. That is, the temperature of molten steel gradually decreases until casting after casting the molten steel in the refining furnace. As nitrogen dissolved in high temperature precipitates into TiN, the nitrogen concentration of STS409L is higher than that of STS409L at the coagulation temperature (1505 ° C) (About 100 ppm at 0.15% Ti).
본 명세서에서 사용한 %는 특히 표시한바가 없더라도 중량%를 의미함은 명백하다.The percentages used in this specification are understood to mean, by weight, unless otherwise indicated.
전기로-AOD(Argon Oxygen Decarburization) 공정으로 스테인레스강을 제조할 때 전기로를 이용하여 합금철 및 일반 스크랩을 용해하는데, 아크(Arc)방전에 의해 공기중의 질소가 용강중으로 용해되기도 하고, 출강시에 용강과 공기의 접촉에 의해 질소가 흡수되어 용강중의 질소농도를 증가시켜 AOD장입전의 질소농도는 200-250PPM 정도가 함유되어 있다. AOD에서는 산소와 아르곤의 혼합가스를 이용하여 전기로에서 제조한 스테인레스강 용강의 탄소를 제거하고 있는데 스테인레스강중의 질소는 이러한 탈탄과정중에 생성되는 CO 가스 기포와 아르곤 가스 기포에 의해 제거되는 것으로 알려져 있으며, AOD 정련로 이후의 공정에서 질소농도를 저감시키는 것은 불가능하므로 정련로내의 정련과정에서 질소농도를 충분히 낮추어야 한다.When producing stainless steel by the electro-furnace (Argon Oxygen Decarburization) process, it dissolves ferroalloys and ordinary scrap using an electric furnace. Nitrogen in air is dissolved in the molten steel by arc discharge, The nitrogen concentration in the molten steel is increased by the absorption of nitrogen by the contact of the molten steel and the air, and the nitrogen concentration before the AOD charging is about 200-250PPM. In AOD, carbon is removed from the stainless steel molten steel produced in an electric furnace by using a mixture gas of oxygen and argon. Nitrogen in stainless steel is known to be removed by CO gas bubbles and argon gas bubbles generated during the decarburization process, Since it is not possible to reduce the nitrogen concentration in the process subsequent to the AOD refining furnace, the nitrogen concentration in the refining furnace must be sufficiently lowered.
용강의 탈질소 반응은 다음의 5가지 소과정으로 나누어 생각할 수 있다.The denitrification of molten steel can be considered in the following five sub-processes.
제1도는 11.5% Cr의 STS강에서의 Ti와 N의 관계를 나타내는 그래프도.FIG. 1 is a graph showing the relationship between Ti and N in 11.5% Cr STS steel. FIG.
제2도는 정련로 종점에서의 질소농도와 제품의 질소농도의 관계를 나타내는 그래프도.FIG. 2 is a graph showing the relationship between the nitrogen concentration at the end point of the refining furnace and the nitrogen concentration of the product. FIG.
제3도는 장입 탄소농도가 질소농도에 미치는 영향을 나타내는 그래프도.FIG. 3 is a graph showing the influence of the loading carbon concentration on the nitrogen concentration. FIG.
제4도는 장입 탄소농도와 탄소픽업량의 관계를 나타내는 그래프도.FIG. 4 is a graph showing the relationship between the charging carbon concentration and the carbon pickup amount; FIG.
제5도는 상취랜스 종점에서의 탄소농도와 질소농도의 관계를 나타내는 그래프도.FIG. 5 is a graph showing the relationship between the carbon concentration and the nitrogen concentration at the extreme lance end point. FIG.
표 2는 본 발명의 적용에 의해 생산된 STS409L의 정련로 종점 및 제품에서의 탄소 및 질소 농도를 나타낸 것으로 탄소, 질소 농도를 극히 낮은 수준까지 낮추는 것이 가능하게 되었으며, 이 결과 연속주조시에 TiN에 의한 침적 노즐막힘 현상을 현저하게 개선할 수 있었다.Table 2 shows the carbon and nitrogen concentration in the end point of the refining furnace and product of STS409L produced by the application of the present invention, and it is made possible to lower the carbon and nitrogen concentration to an extremely low level. As a result, It is possible to remarkably improve the clogging of the immersion nozzle.
본 발명의 목적은, 저탄소, 저질소 Ti 안정화 스테인레스강의 제조시 탄소농도조절상의 문제점을 발생시키지 않으면서 용강중의 질소농도를 효과적으로 낮출 수 있는 스테인레스강 정련방법을 제공하는 것이다.An object of the present invention is to provide a stainless steel refining method capable of effectively lowering the nitrogen concentration in molten steel without causing a problem of carbon concentration control during the production of low carbon and low nitrogen Ti stabilized stainless steels.
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KR1019960031002A KR100384119B1 (en) | 1996-07-29 | 1996-07-29 | Method for refining stainless steel containing low carbon and low nitrogen |
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KR1019960031002A KR100384119B1 (en) | 1996-07-29 | 1996-07-29 | Method for refining stainless steel containing low carbon and low nitrogen |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100363417B1 (en) * | 1998-12-09 | 2003-01-24 | 주식회사 포스코 | Decarburization of Low Carbon Stainless Steel |
KR100523106B1 (en) * | 2001-12-17 | 2005-10-19 | 주식회사 포스코 | method for refining a stainless steel sheet with low nitrogen |
KR100743367B1 (en) * | 2001-07-04 | 2007-07-26 | 주식회사 포스코 | Method of refining low nitrogen, low carbon stainless steel sheets having stabilized titanium |
KR101052262B1 (en) * | 2008-12-24 | 2011-07-27 | 주식회사 포스코 | Low Carbon Steel Manufacturing Method |
KR101400550B1 (en) * | 2012-09-10 | 2014-05-28 | 주식회사 포스코 | High speed decarburization method for high carbon stainless steel |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6026611A (en) * | 1983-07-22 | 1985-02-09 | Nisshin Steel Co Ltd | Manufacture of extra-low nitrogen steel containing cr by refining |
JPS6260813A (en) * | 1985-09-11 | 1987-03-17 | Nippon Kokan Kk <Nkk> | Continuous refining method |
JP3063431B2 (en) * | 1992-11-05 | 2000-07-12 | 住友金属工業株式会社 | Decarburization refining method of molten steel containing chromium |
-
1996
- 1996-07-29 KR KR1019960031002A patent/KR100384119B1/en not_active IP Right Cessation
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100363417B1 (en) * | 1998-12-09 | 2003-01-24 | 주식회사 포스코 | Decarburization of Low Carbon Stainless Steel |
KR100743367B1 (en) * | 2001-07-04 | 2007-07-26 | 주식회사 포스코 | Method of refining low nitrogen, low carbon stainless steel sheets having stabilized titanium |
KR100523106B1 (en) * | 2001-12-17 | 2005-10-19 | 주식회사 포스코 | method for refining a stainless steel sheet with low nitrogen |
KR101052262B1 (en) * | 2008-12-24 | 2011-07-27 | 주식회사 포스코 | Low Carbon Steel Manufacturing Method |
KR101400550B1 (en) * | 2012-09-10 | 2014-05-28 | 주식회사 포스코 | High speed decarburization method for high carbon stainless steel |
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