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Oxygen Steelmaking Introduction MATERIALS 3F03 MARCH 23, 2015
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Hot Metal Chemistry 2 Figure Source: 2 Hot Metal is saturated in C, due to hearth conditions Hot metal in coke bed Typical hot metal chemistry: 4.5 - 5.0 % C 0.3-1.0 % Si 0.1 – 0.7 % Mn 0.05-0.10 % S 0.01-0.08 % P External desulphurization after BF is typical in industry Carbon content of hot metal needs to be substantially lowered to create steel
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Oxygen Steelmaking Refers to augeneous process for converting hot metal into steel: Top blown LD (Linz-Donowitz) BOF (Basic Oxygen Furnace) or BOS Bottom Blown OBM, Q-BOP Combined Blowing KOBM, LBE 4% C to less than 0.1 % C in ~16 minutes (~30 minutes total) 3 Figure Source: 1
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Process Sequence 4 Figure Source: 1
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BOF Blow Usually 16-25 minutes Pure oxygen blown in a supersonic rates generates slag/metal emulsion for high reaction rate ~100% oxygen utilization 5 Figure Source: 1
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Process Reactions There are three major stages in the BOF process: 1) Slag Formation 2) Constant Decarburization Rate 3) Carbon mass transfer control 6 Figure Source: 1
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Slag Formation Soft blowing to start to make a SiO2-FeO rich slag (Fayalitic-type) Once the slag is formed, harder blowing creates slag-metal emulsion Oxidation at the end 7 Figure Source: 1
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Mass and Energy Balance More heat generated from C Oxidation Si Oxidation Than required for: ◦Heating metal ◦Heating and melting slag Coolants added: Scrap (70/30 hot metal ratio common in NA) Iron ore 8 Figure Source: 1
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Mass and Energy Balance 9 Figure Source: 1
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Bottom Blowing Most BOF vessels have some form of bottom stirring to improve mixing: C & O closer to equilibrium Better dephosphorization Quicker slag formation Less iron oxide in slag for better iron and alloy yield Looking at mixing times, a small amount of bottom gas is almost like total bottom flow LH is lance height QB and QT are bottom and top flow rates 10 Figure Source: 1
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Bottom Blowing Lower iron yield loss (as FeO in the steelmaking) associated with bottom blowing C & O closer to equilibrium More decarburization before entering carbon mass transport control regime 11 Figure Source: 1
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OS Reactions Oxygen is the driver for most reactions Controlled by oxygen potential Involve oxygen directly 12 Figure Source: 1
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OS Reactions Oxygen is the driver for most reactions Controlled by oxygen potential Involve oxygen directly 13 Figure Source: 1
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Oxidation of Silicon Rate Controlled by mass transfer of silicon in metal: [Si] + 2(FeO) = (SiO2) + 2[Fe] Shows first order behavior until Si content <0.05% Si Silicon oxidation largely completely in early stages of the blow 14 Figure Source: 1
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Oxidation of Manganese By direct oxidation at hot spot, and: [Mn] + [O] = (MnO) [Mn] + (FeO) = (MnO) + Fe Second reaction predominant later in blow 15 Figure Source: 1
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Oxidation of Phosphorous P2O5 is acidic, so basic slags are required Requires oxidizing conditions Bottom blown processes closer to slag- metal equilibrium Bottom lime injection with O2 Initial slag has high FeO content Mid-blow: FeO content decreases, more reducing conditions in slag Possibility for P reversion back to steel End blow: More oxidizing conditions, opportunity for further phosphorous oxidation 16 Figure Source: 1
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Sulphur Removal Generally poor because of oxidizing conditions S partition is worse with acidic slag s Better to maximize desulphurization in the BF, use external desulphurization facility 17 Figure Source: 1
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Critical Carbon Content Once carbon mass transfer control regime commences: Supply of C to reaction sites is not sufficient to consume O Oxygen dissolution in steel substantially increases Oxidation of Fe increases, higher FeO content in slag Carbon content where constant decarburization regime ends is called Critical Carbon Content 18 Figure Source: 1
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Critical Carbon Content Carbon content where constant decarburization regime ends is called Critical Carbon Content 1 – Slag Formation regime 2- Constant Decarburization rate regime 3- Carbon Mass transport control 19 Figure Source: 1
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Critical Carbon Content Carbon content where constant decarburization regime ends is called Critical Carbon Content Options to reduce critical carbon content: Slower oxygen blowing (productivity impact) 20 Figure Source: 1
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Critical Carbon Content To reduce carbon content lower than the critical carbon content means that higher yield loss of Fe to slag must be accepted Increased oxygen dissolution into steel Other options include vacuum processes for ultra-low carbon grades Reminder: Bottom blowing practice means lower oxidation of metal for a given carbon content 21 Figure Source: 1
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References 1 Bramha Deo and Rob Boom, Fundamentals of Steelmaking Metallurgy, Prentice Hall, 1993, Chapters 5.1-5.2 and 6.1-6.6 2 Geerdes et Al, Blast Furnace Ironmaking: An introduction, 2009 Much of the content is taken directly from or adapted from Materials 4C03 Oxygen Steelmaking slides prepared Dr. Gord Irons.
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