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Ladle Furnace (LF) — Secondary Metallurgy — Secondary Metallurgy process
Secondary MetallurgyChapter 3 of 3 · 7 min

Ladle Furnace (LF) — Secondary Metallurgy

How steel tapped from the BOF or EAF is reheated, desulphurised, and precisely alloyed in a ladle furnace to meet tight composition and temperature targets before continuous casting.

Alloy Additions, Casting Readiness & Vacuum Treatment

Alloy Additions and Trim Chemistry

Alloying in the ladle furnace is the precision step in steel chemistry — the LF is where the final composition window is closed. Bulk additions (ferromanganese, ferrosilicon, ferrochrome) were made at BOF/EAF tapping, deliberately held 10–20% below the final target to allow for trim at the LF without the risk of overalloying. At the LF, trim additions of 5–100 kg (depending on furnace size and specification tightness) fine-tune each element to within ±0.01% of the target.

Ferroalloy dissolution is governed by the same mass transfer principles as desulphurisation: strong argon stirring ensures rapid dissolution and homogeneous distribution. Alloy additions should be completed with adequate arc-off time remaining for a "soft stir" — a period of gentle argon stirring with the arc off to float out any oxide inclusions generated by the dissolution and allow inclusion flotation into the slag before the ladle departs.

For grades requiring very tight tolerances — interstitial-free (IF) automotive steel with <30 ppm C and <30 ppm N, bearing steel with <10 ppm O — the LF prepares the steel to the point where further refinement in the RH or VD degasser is required. The LF cannot remove dissolved gases (hydrogen, nitrogen, excess oxygen) below the limits set by thermodynamic equilibrium at ladle pressure and temperature. This handoff — LF to vacuum degasser — is the defining step for ultra-clean steel grades.

When the LF Hands Off to Vacuum Degassing

After LF treatment, certain steel grades require vacuum degassing to remove dissolved gases that cannot be extracted at atmospheric pressure. The driving force for degassing is thermodynamic: at 1 millibar absolute pressure, the equilibrium dissolved hydrogen in liquid steel is less than 0.5 ppm (vs ~3 ppm at atmospheric pressure), and the equilibrium carbon-oxygen product falls dramatically, enabling ultra-low carbon decarburisation.

Grades requiring vacuum treatment: - Ultra-low carbon (IF steel): Interstitial-free steels for automotive deep drawing require <30 ppm C and <30 ppm N. The RH degasser achieves this by recirculating the steel between the ladle and the vacuum vessel at high rates — up to 150 t/min — through the up-snorkel (argon injection lifts steel up) and the down-snorkel (gravity return). The CO evolution at low pressure drives decarburisation to <10 ppm C in 15–20 minutes. - Ultra-low hydrogen (heavy plate and forging grades): Hydrogen above 2–3 ppm in solidified steel causes flaking — internal hydrogen-induced cracking in heavy sections. VD (vacuum degasser) or RH treatment to <2 ppm H₂ is mandatory for plate thicknesses above 50 mm. H₂ degassing is rapid at vacuum: 15–20 minutes suffices for most applications. - Ultra-low nitrogen (<50 ppm N for electrical steel): Nitrogen is the most difficult dissolved gas to remove because N₂ desorption kinetics are slower than CO or H₂ desorption. Achieving <50 ppm N requires a combination of EAF practice (sealed tapping, argon shrouding), careful LF slag management, and VD treatment. Full nitrogen removal to <30 ppm is rare and expensive. - Ultra-low total oxygen (<10 ppm for bearing steel): RH-OB (oxygen blowing) is used for bearing grades: oxygen is injected into the RH vessel to react with excess aluminium and carbon, generating CO evolution that flushes oxygen and inclusions upward into the slag layer. A 20–30 minute RH-OB treatment achieves <10 ppm total oxygen.

RH vs VD comparison: The RH degasser is the high-throughput workhorse — it can treat 300 t in 20–30 minutes, inject alloys and oxygen under vacuum, and integrate directly with the casting sequence. The VD (vacuum tank degasser) is simpler in concept (the ladle is placed in a sealed vessel under vacuum, with argon stirring through the bottom plugs) and is highly effective for hydrogen removal at lower capital cost. VD is preferred for heavy plate and forging shops where hydrogen removal is the primary target; RH is preferred for high-volume flat-rolled production where ultra-low carbon is required.

Key ladle furnace terms

Tap each card to reveal the definition.

Tap to revealWhite slag
AnswerLF slag with FeO <0.5%, visible as white or pale yellow colour. Indicates a well-reduced, highly basic slag with high sulphide capacity and low reoxidation potential. The operational target for clean steel production.
Tap to revealCaSi wire
AnswerCalcium silicide wire injected through a hollow lance at 80–150 m/min. Releases calcium into the steel bath to desulphurise and to modify solid Al₂O₃ inclusions into liquid calcium aluminates, preventing SEN clogging.
Tap to revealArgon rinsing
AnswerGentle argon stirring through ladle bottom purgeplugs (soft stir), typically at the end of LF treatment before departure to the caster. Promotes inclusion flotation without reintroducing air oxygen or disrupting the slag layer.
Tap to revealSynthetic slag
AnswerA pre-blended flux addition (lime, alumina, fluorspar) added to the ladle at tapping to immediately establish the correct LF slag chemistry, shortening the time required to achieve the reducing white slag condition.
Tap to revealSulphide capacity
AnswerA thermodynamic measure of a slag's ability to hold sulphur in solution. Increases with basicity (CaO/SiO₂) and temperature, and with reduction of FeO to <1%. Quantified as Cs = (%S)·(pO₂/pS₂)^0.5.
Tap to revealTrim addition
AnswerA small, precise ferroalloy addition at the LF to close the composition window to specification. Typically 5–100 kg of ferroalloy for a 150–300 t heat. Made after bulk alloying at tapping has brought composition to within ~80% of target.

Key ladle furnace operating parameters

paramvalue
Ladle capacity80–350 t
Transformer rating20–60 MVA
Heating rate3–5 °C/min
Arc-on time10–40 min
Total treatment time20–60 min
Sulphur removal target<0.005% (standard); <0.001% (ultra-low)
FeO in slag (target)<1% (white slag condition)
Slag basicity targetCaO/SiO₂ = 3–5
Argon stirring flow (arc-on)3–8 NL/min·t
Argon soft stir (arc-off)0.5–2 NL/min·t
Temperature window to caster±5–10 °C
Electrode consumption0.3–0.8 kg/t

Typical parameters for a 150–300 t ladle furnace at a modern integrated or EAF steelplant.

The ladle furnace enables tight chemistry windows that the BOF and EAF cannot achieve alone

Modern steel specifications — particularly for automotive, linepipe, bearing, and electrical grades — require composition tolerances of ±0.01–0.02% on multiple elements simultaneously, with sulphur <0.005% and dissolved oxygen <20 ppm. Neither the BOF nor the EAF can achieve these windows in the primary vessel: the intense reactions and high temperatures are incompatible with the precision required. The LF, operating at 1,580–1,620 °C with controlled stirring and reducing slag, is the only practical environment for closing these windows before casting.

Key Facts

The ladle furnace was commercialised in 1971 and is now universal in quality steelmaking — every flat-rolled and tubular steel plant uses LF secondary metallurgy between the primary furnace and the continuous caster.

LF heating rates of 3–5 °C/min allow precise temperature targeting at the caster — the tapping temperature from the BOF/EAF can be deliberately set 30–60 °C below the caster optimum, with the LF making up the difference.

Desulphurisation from 0.020% to <0.001% is achievable in 20–40 minutes of LF treatment using a reducing (white) slag with CaO/SiO₂ of 3–5 and strong argon stirring — the kinetics are driven by mass transfer across the steel-slag interface.

Calcium wire injection modifies solid Al₂O₃ inclusions (formed by aluminium deoxidation) into liquid calcium aluminates, preventing submerged entry nozzle clogging at the continuous caster — a prerequisite for continuous sequence casting of clean steel.

The LF deliberately receives steel with composition 10–20% short of specification target, with final trim additions made at the LF — this strategy avoids the risk of overalloying in the turbulent BOF/EAF environment where precise additions are difficult.

Electrode consumption in the LF (0.3–0.8 kg/t) is 3–5 times lower than in the EAF, reflecting the lower power density and the absence of scrap melting loads on the electrode.

Glossary

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