NivaarExam PrepOfficial exam papers ↗

21-Mat-A3 Structure and Characterization of Materials · May 2018

Question 5 of 7: Iron and Steelmaking (20 marks)

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

Notes on this paper

Paper format. National Exams, May 2018 — 10-Met-A3, Metal Extraction Processes. Three hours, closed book, one approved calculator (Casio or Sharp). Seven problems of 20 marks each; the rubric asks for any five, and only the first five in the answer book are marked. All seven are solved here, because this set is a study resource rather than an exam script.

Note on the exam title. The printed exam header reads 10-Met-A3, Metal Extraction Processes. The content is extractive metallurgy — mineral processing, mass and heat balances, pyrometallurgical roasting, zinc production, ironmaking and electrometallurgy — and is answered as such.

Reference texts. The answers below are keyed to the works normally recommended for this syllabus code:



Question 5 — Iron and Steelmaking (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.

Iron blast furnace: feeds, zones and productsStack 400–900 °CFe₂O₃ + 3 CO → 2 Fe + 3 CO₂Bosh 900–1300 °CC + CO₂ → 2 CO (Boudouard)Tuyere / raceway ~2000 °C2 C + O₂ → 2 COHearth ~1500 °CCharge: iron ore + coke + limestoneTop gas (CO, CO₂, N₂)Hot blastSlag tapHot metalslag layerhot metal (~4 % C)Coke is fuel, reductant and the permeable burden support; limestone fluxes the gangue
Figure 5.1 — The blast furnace as a counter-current shaft reactor: burden descends, hot reducing gas ascends, and the reaction each zone performs is set by its temperature.

(a) Three major feed materials. The burden charged at the top of a blast furnace consists of iron-bearing material — sinter, pellets or lump ore, essentially Fe2O3 and Fe3O4; metallurgical coke; and flux, normally limestone (CaCO3) with dolomite where magnesia is wanted in the slag. A fourth feed enters at the bottom: the hot blast of preheated air, together with injected auxiliary fuel such as pulverised coal.

(b) The function of coke. Coke performs four distinct duties. First, it is the fuel: burning at the tuyeres, $\mathrm{2\,C + O_2 \rightarrow 2\,CO}$, it releases the heat that raises the burden to reaction temperature and melts iron and slag, generating raceway temperatures near 2000 °C. Second, it is the source of the reducing gas: that combustion produces CO, which does the bulk of the reduction as it ascends the stack, $\mathrm{Fe_2O_3+3\,CO\rightarrow2\,Fe+3\,CO_2}$. Third, it is the direct reductant at high temperature via the Boudouard reaction, $\mathrm{C+CO_2\rightarrow2\,CO}$, which becomes favourable above about 1000 °C and also carburises the iron, giving hot metal its characteristic 4 % carbon and a melting point some 350 °C below pure iron's. Fourth, coke is the only burden component that stays solid all the way to the hearth, so it provides the permeable skeleton through which gas ascends and liquid iron/slag descend — without it the furnace would choke.

(c) The function of limestone. Limestone is the flux. It calcines in the stack, $\mathrm{CaCO_3\rightarrow CaO+CO_2}$, and the lime combines with the acidic gangue (mainly silica and alumina) to form a fluid, low-melting slag, $\mathrm{CaO+SiO_2\rightarrow CaSiO_3}$. The slag collects gangue and coke ash for tapping, absorbs sulphur from the metal (the furnace's main desulphurising route), and, floating on the hot metal, protects it from re-oxidation.

(d) The products. Three streams leave the furnace: hot metal (pig iron), tapped near 1500 °C carrying roughly 4–4.5 % C plus Si, Mn, P and S; the slag, a calcium aluminosilicate sold as a cement supplement or aggregate; and the top gas, leaving at 100–250 °C with about 20–25 % CO and 20 % CO2, cleaned and burned in the hot-blast stoves and power plant.

(e) Advantages of oxygen over air in steelmaking. The case rests on removing the nitrogen that makes up 79 % of air. Thermally, every mole of oxygen delivered as air drags 3.76 mol of nitrogen that must be heated and vented; eliminating it leaves enough heat surplus for a basic oxygen furnace to run on the chemical energy of the blow alone and absorb 25–30 % scrap as coolant. Kinetically, oxygen reaches the bath at much higher partial pressure without the diluent, so decarburisation is far faster — a 300 t heat blows in about 20 minutes, against eight to ten hours for the open-hearth process it displaced. On metallurgical quality, dissolved nitrogen drops to 20–40 ppm from 60–120 ppm for air-blown steel, avoiding strain-ageing embrittlement. And on the environmental/off-gas side, gas volume to be cleaned falls roughly fourfold and the off-gas becomes a concentrated, recoverable CO stream.

(f) Deoxidation of steel. At the end of the oxygen blow the bath carries 400–800 ppm dissolved oxygen; left in, it would react with carbon on freezing, $\mathrm{[C]+[O]\rightarrow CO(g)}$, blowing gas and porosity into the ingot. Deoxidation ("killing") adds elements with greater oxygen affinity than iron so a stable oxide forms and floats to the slag, in ascending strength: manganese ($\mathrm{Mn+[O]\rightarrow MnO}$, weakest, cheapest, also fixes sulphur as MnS); silicon ($\mathrm{Si+2\,[O]\rightarrow SiO_2}$, usually with Mn since the resulting silicate is liquid and separates readily); and aluminium ($\mathrm{2\,Al+3\,[O]\rightarrow Al_2O_3}$, strongest, defining a "fully killed" steel, with residual Al also pinning austenite grain size via AlN).

Summary — Question 5
PartAnswer in brief
(a) FeedsIron ore (sinter/pellets/lump), metallurgical coke, limestone flux — plus the hot blast
(b) CokeFuel; source of CO reducing gas; direct reductant/carburiser via Boudouard; permeable support
(c) LimestoneCalcines to CaO, fluxes silica/alumina to a fluid basic slag, absorbs sulphur, protects the metal
(d) ProductsHot metal (~4 % C at ~1500 °C), slag, and top gas
(e) Oxygen vs airNo nitrogen ballast → heat surplus/scrap capacity, ~20 min blows, N in steel 20–40 ppm, 1/4 off-gas volume
(f) DeoxidisersMn, Si, Al — higher oxygen affinity than Fe, applied in ascending strength