KR840008921A - Method of manufacturing chromium-containing steel - Google Patents

Method of manufacturing chromium-containing steel Download PDF

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KR840008921A
KR840008921A KR1019840002639A KR840002639A KR840008921A KR 840008921 A KR840008921 A KR 840008921A KR 1019840002639 A KR1019840002639 A KR 1019840002639A KR 840002639 A KR840002639 A KR 840002639A KR 840008921 A KR840008921 A KR 840008921A
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weight
oxygen
molten iron
compound selected
blowing
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KR1019840002639A
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KR910009961B1 (en
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다까시(외3) 야마우찌
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아베 유즈루(외1)
닛신 세이꼬오 가부시기 가이샤
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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/005Manufacture of stainless steel
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/04Removing impurities by adding a treating agent
    • C21C7/068Decarburising
    • C21C7/0685Decarburising of stainless steel

Abstract

내용 없음No content

Description

지P함유크롬강의 제조방법Method of manufacturing chromium-containing steel

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

Claims (9)

C의 중량으로 4.5%이하, P 의 중량으로 적어도 0.010% 및 Cr의 중량으로 적어도 3.0%를 함유한 크롬함유용선부터 출발하여, 산소의 정부 불어넣기에 적용된 랭스와 단독 또는 혼합으로 산소 및 비산소계가스의 저부 붙어넣기에 적용된 2중관 구조의 적이도 하나의 바람구멍이 구비된 용기에서,Starting with a chromium-containing charter containing less than 4.5% by weight of C, at least 0.010% by weight of P, and at least 3.0% by weight of Cr, oxygen and non-oxygen-based In a vessel equipped with a single duct of air with a double tube structure applied to the bottom attachment of the gas, (가) 아래 단계 라항의 끝에서 중량으로 적어도 4.5%의 탄소함유량의 크롬함유용선을 제공하는데 충분한 양으로 용기내의 크롬함유용선에 고체탄소원을 첨가하고,(A) adding a solid carbon source to the chromium-containing molten iron in the vessel in an amount sufficient to provide a chromium-containing molten iron of at least 4.5% by weight at the end of step d. (나) 비산소계 가스를 그것에 전부 불어넣기에 의하여 용기내의 내용물을 교반하고,(B) stir the contents in the container by blowing all of the non-oxygen-based gas into it; (다) C의 중량으로 적어도 4.5%와 Si의 중량으로 0.15% 이하를 함유한 1500℃ 및 1700℃간의 온도범위의 크롬함유용선을 제공하게 용선에 산소를 불어넣고,(C) oxygen is blown into the molten iron to provide a chromium-containing molten iron in the temperature range between 1500 ° C. and 1700 ° C. containing at least 4.5% by weight of C and 0.15% or less by weight of Si, (라) 용기부터 선행단계로 형성된 슬랙을 실질적으로 제거하고,(D) substantially removing the slag formed in the preceding step from the vessel; (마) 용기내의 용선에 탈 P 플럭스를 첨가하고,(E) add de-P flux to the molten iron in the vessel, (바) 중량으로 적어도 1.0%의 레벨로 슬랙내의 산화철의 농도를 유지하면서 형성된 슬랙과 융선의 효과적인 접촉을 촉진하게 비산소계 가스를 그것에 저부 불어넣기에 의하여 용기내의 내용물을 교반하고,(F) stirring the contents in the vessel by blowing a non-oxygen based gas into it to promote effective contact of the slag formed with the slag while maintaining the concentration of iron oxide in the slag at a level of at least 1.0% by weight; (사) 용기부터 슬랙을 실질적으로 제거하고,(G) substantially removing the slack from the container, (아) 비산소계 가스를 그것에 지부로 불어넣으면서 탈탄을 위하여 용기내의 용신에 산소를 불어넣는 단계를 가지는 것을 특징으로 하는 저P함유크롬강의 제조방법.(H) A method for producing a low P-containing chromium steel, comprising the step of blowing oxygen into a solvent in a container for decarburization while blowing a non-oxygen gas into a branch thereof. 제1항에 있어서, 탈P플럭스는 알칼리로 금속의 불화를 및 염화물부터 선택된 적어도 하나의 화합물의 중량으로 30-80%, 리륨 산화물 및 리륨탄산염부터 선택된 적어도 하나의 화합물의 중량으로 0.4내지 30%산화철 및 산화니켈부터 선택된 적어도 하나의 화합물의 중량으로 5 내지 50% 및 알칼리로 금속의 산화물 및 탄산염부터 선택된 적어도 하나의 화합물의 중량으로 0-40%을 가지는 것.The de-P flux is 30-80% by weight of at least one compound selected from fluoride and chlorides, and from 0.4 to 30% by weight of at least one compound selected from lithium oxide and lithium carbonate. Having from 5 to 50% by weight of at least one compound selected from iron oxides and nickel oxide and from 0 to 40% by weight of at least one compound selected from oxides and carbonates of metals with alkalis. 제1항에 있어서 단계바항의 적어도 최후부분은 용기내의 내용물에 산소를 정부로 불어놓으면서 수행되고 그것에 의하여 중량으로 적어도 1.0%의 레벨로 슬랙내의 산화철의 농도를 유지하는 것.The process of claim 1, wherein at least the last part of the step bar is carried out by blowing oxygen into the contents of the container to thereby maintain the concentration of iron oxide in the slack at a level of at least 1.0% by weight. 제3항에 있어서, 탈P용 플럭스는 알칼리로 금속의 불화물 및 염화물부터 선택된 적어도 하나의 화합물의 중량으로 30-80%, 리륨산화물 및 리륨탄산염부터 선택된 적어도 하나의 화합물의 중량으로 0.4-30%, 산화철 및 산화니켈부터 선택된 적어도 하나의 화합물의 중량으로 5-50% 및 알칼리로 금속의 산화물 및탄산염부터 선택된 적어도 하나의 화합물의 중량으로 0-40%를 가지는 것.4. The dephosphorization flux of claim 3 is 30-80% by weight of at least one compound selected from fluorides and chlorides of metals with alkali, and 0.4-30% by weight of at least one compound selected from lithium oxides and lithium carbonates. , 5-50% by weight of at least one compound selected from iron oxides and nickel oxide and 0-40% by weight of at least one compound selected from oxides and carbonates of metals with alkalis. C의 중량으로 4.5% 이하, P의 중량으로 적어도 0.010% 및 Cr의 중량으로 적어도 3.0%를 함유한 크롬함유 용선부터 출발하여 산소의 정부 불어넣기에 적용된 랭스와 단독 또는 혼합으로 산소 및 비산소개가스의 저부 불어넣기에 적용된 2중관 구조의 적어도 하나의 바람구멍이 구비된 용기에서,Oxygen and fugitive introduction gases, either alone or in combination with a lance which is applied to the government blowing of oxygen, starting from a chromium-containing molten iron containing 4.5% or less by weight of C, at least 0.010% by weight of P and at least 3.0% by weight of Cr In a vessel equipped with at least one air hole of a double tube structure applied to the bottom blowing of (가) 아래 라항의 단개끝에서 중량으로 적어도 4.5%의 탄소함유량의 크롬함유용선을 제공하는데 충분한 양으로 용기내의 크롬함유 용선에 고체탄소원을 첨가하고,(A) adding a solid carbon source to the chromium-containing molten iron in the vessel in an amount sufficient to provide a chromium-containing molten iron of at least 4.5% by weight at the end of d) (나) 비산소계 가스를 그것에 저부 불어넣기에 의하여 용기내의 내용물을 교반하고,(B) stirring the contents in the container by blowing a non-oxygen-based gas into it, (다) C의 중량으로 적어도 4.5%와 Si의 중량으로 0.15% 이하를 함유한 1500℃ 및 1700℃간의 온도범위의 크롬함유 용선을 제공하게 용선에 산소를 불어넣고,(C) oxygen is blown into the molten iron to provide a chromium-containing molten iron in the temperature range between 1500 ° C and 1700 ° C containing at least 4.5% by weight of C and 0.15% or less by weight of Si, (라) 용기부터 선행단계로 형성된 슬랙을 실질적으로 제거하고,(D) substantially removing the slag formed in the preceding step from the vessel; (마) 용기내의 용선에 탈 P 플럭스를 첨가하고,(E) add de-P flux to the molten iron in the vessel, (바) 중량으로 적어도 1.0%의 레벨로 슬랙내의 산화철의 농도를 유지하면서 형성된 슬랙과 용선의 효과적인 접촉을 촉진하게 비산소계가스를 그것에 저부 불어넣기에 의하여 용기내의 내용물을 교반하고,(F) stirring the contents in the container by blowing non-oxygen based gas to it to promote effective contact of the slag formed with molten iron while maintaining the concentration of iron oxide in the slag at a level of at least 1.0% by weight; (사) 용기부터 슬랙을 실질적으로 제거하고,(G) substantially removing the slack from the container, (아) 비산소계 가스를 그것에 지부를 불어넣으면서 탈탄을 위하여 용기내의 용선에 산소를 불어넣고,(H) blowing oxygen into the molten iron in the container for decarburization, blowing non-oxygen-based gas into it; (자) P는 소망되는 레벨이 도달될 때까지 용선의 탄소함유량을 중량으로 4.5% 이상으로, 실리콘 함유량을 중량으로 0.15% 이하로 조절하면서 산소불어넣기로 1500℃ 내지 1700℃간의 온도범위로 용선의 온도를 상승시키는 연속사이클 사이의 중, 단계를 가지고 단계 마, 바 및 사항의 사이클을 반복하는 단계를 가지는 것을 특징으로 하는 지P함유크롬강의 제조방법.(I) P is a molten iron in the temperature range of 1500 ° C to 1700 ° C by oxygen blowing while adjusting the carbon content of the molten iron to 4.5% or more by weight and the silicon content to 0.15% or less by weight until the desired level is reached. A method for producing chromium-containing steel, characterized in that it has a step of repeating the cycle of the step e, bar, and the matter between the continuous cycle of raising the temperature of. 제5항에 있어서 탈P용 플럭스는 알칼리로 금속의 불화물 및 염화물부터 선택된 적어도 하나의 화합물의 중량으로 30-80%, 리륨산화물 및 리륨산염부터 선택된 적어도 하나의 화합물의 중량으로 0.4-30% 산화철 및 산화니켈부터 선택된 적어도 하나의 화합물의 중량으로 5-50% 및 알칼리로 금속의 산화물 및 탄산염부터 선택된 적어도 하나의 화합물의 중량으로 0-40%를 가지는 것.The flux for deplating according to claim 5 is 30-80% by weight of at least one compound selected from fluorides and chlorides of metals with alkali, and 0.4-30% by weight of at least one compound selected from lithium oxides and lithium salts. And 5-50% by weight of at least one compound selected from nickel oxide and 0-40% by weight of at least one compound selected from oxides and carbonates of metals with alkalis. 제5항에 있어서, 용선의 온도를 상승시키는 적어도 하나의 중간단계에서 용선은 그것에 첨가된 산화발열채를 가지고 수행되는 것.6. The molten iron according to claim 5, wherein the molten iron is performed with an oxidative heating element added thereto in at least one intermediate step of raising the temperature of the molten iron. 제5항에 있어서, 단계바항의 적어도 최종부분은 용기의 내용물에 산소를 정부로 불어넣으면서 중량으로 적어도 1.0%의 레벨에서 슬랙내의 산화철의 농도를 유지하면서 수행되는 것.6. The process of claim 5, wherein at least the final portion of step bar is performed while maintaining oxygen concentration in the slack at a level of at least 1.0% by weight while blowing oxygen into the contents of the vessel. 제8항에 있어서 탈P용 플럭스는 알칼리로 금속의 불화물 및 염화물부터 선택된 적어도 하나의 화합물의 중량으로 30-80%, 리륨산화물 및 리륨탄산염부터 선택된 적어도 하나의 화합물의 중량으로 0.4-30%, 산화질 및 산화니켈부터 선택된 적어도 하나의 화합물의 중량으로 5-50% 및 알칼리로 금속의 산화를 및 탄산염부터 선택된 적어도 하나의 화합물의 중량으로 0-40%를 가지는 것.The flux for deamination according to claim 8 is 30-80% by weight of at least one compound selected from fluorides and chlorides of metals with alkali, 0.4-30% by weight of at least one compound selected from lithium oxide and lithium carbonate, 5-50% by weight of at least one compound selected from oxynitride and nickel oxide and oxidation of metal with alkali and 0-40% by weight of at least one compound selected from carbonates. ※참고사항:최초출원 내용에 의하여 공개하는 것임.※ Note: This is to be disclosed based on the first application.
KR1019840002639A 1983-05-18 1984-05-16 Process for producing low p chromium-containing steel KR910009961B1 (en)

Applications Claiming Priority (2)

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JP58087296A JPS59211519A (en) 1983-05-18 1983-05-18 Production of low p-containing chromium steel
JP87296 1983-05-18

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KR910009961B1 KR910009961B1 (en) 1991-12-07

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DE (1) DE3418643C2 (en)
ES (1) ES532584A0 (en)
FR (1) FR2546182B1 (en)
GB (1) GB2141739B (en)
IT (1) IT1179669B (en)
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DE102005032929A1 (en) * 2004-11-12 2006-05-18 Sms Demag Ag Production of stainless steel of the ferritic steel group AISI 4xx in an AOD converter
DE102006056672A1 (en) 2006-11-30 2008-06-05 Sms Demag Ag Method and apparatus for stainless steel production without electrical energy supply based on pig iron
DE102006056671A1 (en) * 2006-11-30 2008-06-05 Sms Demag Ag Method and apparatus for stainless steel production without electrical energy supply on the basis of pig iron pretreated in a DDD plant
DE102007015585A1 (en) * 2007-03-29 2008-10-02 M.K.N. Technologies Gmbh Melt metallurgical process for producing molten metals and transition metal-containing aggregate for use therein
CN114875211B (en) * 2022-05-18 2023-10-31 山西太钢不锈钢股份有限公司 Method for smelting stainless steel and efficiently desilicating

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FR2546182A1 (en) 1984-11-23
JPS59211519A (en) 1984-11-30
IT1179669B (en) 1987-09-16
SE459184B (en) 1989-06-12
ES8603583A1 (en) 1985-12-16
FR2546182B1 (en) 1989-02-17
IT8467492A1 (en) 1985-11-17
GB2141739B (en) 1986-04-09
GB8412791D0 (en) 1984-06-27
SE8402668L (en) 1984-11-19
IT8467492A0 (en) 1984-05-17
KR910009961B1 (en) 1991-12-07
DE3418643C2 (en) 1994-03-24
DE3418643A1 (en) 1984-11-22
SE8402668D0 (en) 1984-05-17
GB2141739A (en) 1985-01-03
ES532584A0 (en) 1985-12-16
JPS6213405B2 (en) 1987-03-26

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