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21-Mat-A2 Materials Transport Phenomena · December 2013

Question 6 of 9: BOF Cold-Scrap Melting Heat Balance

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

National Exams — December 2013 — Met-A2, Metallurgical Rate Phenomena. Three-hour, closed-book exam using an approved (Casio or Sharp) calculator, one double-sided aid sheet permitted; candidates were told to state any interpretive assumptions. Candidates answer Question 1 plus any four of Questions 2–9 — all nine are solved below for completeness. All questions are of equal value (20 marks each, five questions = 100%).

Reference texts: Geankoplis, C. J., Transport Processes and Separation Process Principles — mass/heat/momentum transfer fundamentals (Fick's/Newton's/Fourier's laws, boundary-layer correlations); Szekely, J. & Themelis, N. J., Rate Phenomena in Process Metallurgy — gas-halo diffusion, ladle/tundish fluid flow, wire injection; Turkdogan, E. T., Fundamentals of Steelmaking — BOF/EAF heat and mass balances; Callister, W. D., Materials Science and Engineering — TTT/CCT diagrams and phase transformations; Incropera, F. P. & DeWitt, D. P., Fundamentals of Heat and Mass Transfer — liquid-metal (low-Pr) convection correlations.

Question 6: BOF Cold-Scrap Melting Heat Balance (20 marks)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Check: the source states 28% scrap in the opening sentence and 30% in the follow-up question. Both parts below use the single figure quoted alongside the temperature-limit statement, 28%, treating the second mention as the same referent rather than an independent value.

Given. Basis: 1 tonne (1000 kg) of charge, scrap fraction $x=0.28$. Scrap heats from $T_{room}=20\,{}^{\circ}\text{C}$ through melting at $T_m=1520\,{}^{\circ}\text{C}$ to bath temperature $T_{bath}=1600\,{}^{\circ}\text{C}$: $C_{p,s}=450$, $C_{p,l}=717$ J/kg K, $L=271{,}000$ J/kg. Heat comes from the hot-metal (liquid steel) sensible heat, $C_{p,l}=717$ J/kg K.

Find. Heat absorbed per tonne of scrap heated/melted to 1600°C; the hot-metal temperature rise (and resulting turn-down temperature) had that scrap fraction not been added.

Approach. Three-stage sensible+latent heat balance for the scrap (solid heating, melting, liquid superheat) gives the MJ/tonne figure directly; energy conservation then says that same heat, if not absorbed by scrap, stays in the hot-metal bath and raises its sensible temperature instead.

  1. Stage 1 — heat solid scrap from room temperature to its melting point. Per tonne (1000 kg) of scrap: $$Q_1=mC_{p,s}\Delta T=(1000)(450)(1520-20)=675\times10^6\ \text{J}=675\ \text{MJ}$$
  2. Stage 2 — latent heat of melting. $$Q_2=mL=(1000)(271{,}000)=271\times10^6\ \text{J}=271\ \text{MJ}$$
  3. Stage 3 — superheat the melted scrap from $T_m$ to bath temperature. $$Q_3=mC_{p,l}\Delta T=(1000)(717)(1600-1520)=57.4\times10^6\ \text{J}=57.4\ \text{MJ}$$
  4. Total heat absorbed per tonne of scrap. $$Q_{total}=Q_1+Q_2+Q_3=675+271+57.4$$ $$\boxed{Q_{total}=1003\ \text{MJ/tonne scrap}}$$
  5. If the 28% scrap fraction had not been added. Per tonne of total charge, scrap absorbs $Q_{scrap}=0.28\times1003=280.9$ MJ, drawn from the sensible heat of the remaining $0.72\times1000=720$ kg of liquid hot metal. Removing that heat sink lets the same heat raise the hot-metal temperature instead: $$\Delta T=\dfrac{Q_{scrap}}{m_{hotmetal}C_{p,l}}=\dfrac{280.9\times10^6}{(720)(717)}$$ $$\boxed{\Delta T=544\ ^{\circ}\text{C}\ \Rightarrow\ T_{final}\approx1600+544=2144\,{}^{\circ}\text{C}}$$

This 544°C excursion is a theoretical energy-balance result testing the concept — scrap as a heat sink limiting turn-down temperature — rather than a physically-observed operating point: in practice a real BOF would never be allowed to reach 2144°C (well above practical refractory and metallurgical limits), which is exactly why the 28% cold-scrap addition, or an equivalent coolant, is a mandatory part of the charge balance.

Question 6 — final results
QuantityValue
Solid sensible heat (Stage 1)675 MJ/tonne scrap
Latent heat of melting (Stage 2)271 MJ/tonne scrap
Liquid superheat (Stage 3)57.4 MJ/tonne scrap
Total heat absorbed by scrap1003 MJ/tonne scrap
Hot-metal temperature rise without scrap≈ 544°C (→ ≈2144°C)