General Principles of Metallurgy
Apply concepts from General Principles of Metallurgy to problem-solving. Focus on numerical practice, shortcuts, and real-world applications.
Concept Core
Metallurgy is the science of extracting metals from their ores and refining them for use. The process follows a general sequence: mining → concentration of ore → extraction (reduction) → refining → alloy making.
Occurrence of Metals
Metals occur in nature as: (1) Native/free state — noble metals like Au, Ag, Pt (low reactivity). (2) Combined state — most metals as oxides (haematite Fe2O3, bauxite Al2O3.2H2O), sulphides (galena PbS, zinc blende ZnS, copper pyrites CuFeS2), carbonates (limestone CaCO3, siderite FeCO3), halides (fluorspar CaF2, rock salt NaCl), silicates.
Minerals vs Ores: A mineral is any naturally occurring compound of a metal. An ore is a mineral from which the metal can be extracted profitably. All ores are minerals but not all minerals are ores.
Concentration (Enrichment) of Ore
The process of removing gangue (earthy impurities) from the ore:
1. Gravity separation (hydraulic washing): Based on density difference. Lighter gangue is washed away by water. Used for oxide ores (tin stone SnO2, haematite Fe2O3).
2. Magnetic separation: Ore or gangue is magnetic. Magnetic material attracted to electromagnetic belt roller. Used for: chromite (magnetic) from siliceous gangue; tin stone (non-magnetic) from wolframite (magnetic) impurity.
3. Froth flotation: For sulphide ores. Powdered ore + water + pine oil + frother (cresol). Sulphide particles (hydrophobic) attach to oil-coated air bubbles and float as froth; gangue (hydrophilic) sinks. Selective flotation of mixed ores using depressants (NaCN depresses ZnS by forming Na2[Zn(CN)4] surface layer, allowing PbS to float first).
4. Leaching (chemical): Dissolving ore selectively. Bauxite: Bayer's process — Al2O3.2H2O + 2NaOH → 2NaAlO2 + 3H2O (dissolves Al2O3, rejects Fe2O3/SiO2). NaAlO2 + CO2 + 2H2O → Al(OH)3 + NaHCO3. Al(OH)3 heated → Al2O3. Gold: cyanide process — 4Au + 8NaCN + 2H2O + O2 → 4Na[Au(CN)2] + 4NaOH. Gold recovered by Zn displacement: 2Na[Au(CN)2] + Zn → Na2[Zn(CN)4] + 2Au.
Extraction of Crude Metal
Thermodynamic Principles: Metal oxide reduction depends on Gibbs free energy change ( G = H - T. S). A reaction is feasible when G is negative.
Ellingham Diagram: Plot of G of oxide formation vs temperature. Key features:
- Lines slope upward (positive slope) because oxidation produces fewer gas molecules (S decreases).
- At the intersection point, two metals have equal G — above this temperature, the lower metal can reduce the upper metal's oxide.
- Carbon line has negative slope (C + O2 → CO2, S ≈ 0; but 2C + O2 → 2CO, S positive → steeper negative slope). Carbon becomes a better reducing agent at higher temperatures.
- Al line is very low (Al2O3 very stable) → aluminium can reduce almost any metal oxide (thermite reaction).
Reduction Methods:
- Carbon reduction (smelting): For oxides of Zn, Fe, Sn, Pb. ZnO + C → Zn + CO (at ~1673 K). Fe2O3 is reduced in blast furnace with coke.
- Aluminium reduction (thermite/aluminothermy): For Cr2O3, Mn3O4, Fe2O3. Cr2O3 + 2Al → Al2O3 + 2Cr. Very exothermic.
- Electrolytic reduction: For highly electropositive metals (Na, K, Ca, Mg, Al). These cannot be reduced by C or H2. Al: Hall-Heroult process (electrolysis of Al2O3 dissolved in cryolite Na3AlF6).
- Self-reduction (auto-reduction): For Cu and Pb from sulphide ores. 2Cu2S + 3O2 → 2Cu2O + 2SO2; Cu2S + 2Cu2O → 6Cu + SO2. The metal sulphide and oxide react to give metal.
Blast Furnace — Iron Extraction
Charge: Fe2O3 (haematite) + coke (C) + limestone (CaCO3, flux). Temperature zones from bottom to top:
| Zone | Temperature | Reaction |
|---|---|---|
| Combustion | ~2000 K | C + O2 → CO2 (exothermic) |
| Reducing | ~1200 K | CO2 + C → 2CO; Fe2O3 + 3CO → 2Fe + 3CO2 |
| Slag formation | ~1500 K | CaCO3 → CaO + CO2; CaO + SiO2 → CaSiO3 (slag) |
| Charge zone | ~500-800 K | Fe2O3 + CO → Fe3O4 → FeO → Fe (stepwise) |
Products: Pig iron (4% C, brittle) → cast iron (3% C) → wrought iron (<0.2% C, malleable). Steel (0.2-2% C) is intermediate.
Refining of Crude Metal
1. Distillation: For volatile metals (Zn, Hg). Crude metal heated; metal vaporises, condenses separately.
2. Liquation: For low-melting metals (Sn, Pb, Bi). Crude metal heated gently; pure metal melts and flows away from higher-melting impurities.
3. Electrolytic refining: Most widely used. Impure metal = anode, pure metal = cathode, soluble salt of metal = electrolyte. Anode dissolves: Cu → + + 2e-. Cathode deposits: + + 2e- → Cu (pure). Impurities settle as anode mud. Used for Cu, Ag, Au, Al, Zn.
4. Zone refining: For ultra-pure metals (Ge, Si, Ga, In). Based on principle that impurities are more soluble in molten metal than in solid. A narrow molten zone is moved along a metal rod; impurities concentrate at one end.
5. Vapour phase refining: (a) Mond process (Ni): Ni + 4CO → Ni(CO)4 (volatile, 330 K) → Ni + 4CO (decomposed at 450 K). (b) Van Arkel process (Zr, Ti): Zr + 2I2 → ZrI4 (volatile, 870 K) → Zr + 2I2 (decomposed at 1800 K on hot W filament).
Specific Metal Extractions
Copper: From CuFeS2 (copper pyrites). Concentrated by froth flotation → roasted (2CuFeS2 + O2 → Cu2S + 2FeS + SO2) → smelted with SiO2 flux (FeS + SiO2 → FeSiO3 slag) → self-reduction (2Cu2S + 3O2 → 2Cu2O + 2SO2; Cu2S + 2Cu2O → 6Cu + SO2) → blister copper (98.5%) → electrolytic refining → 99.99% Cu.
Aluminium: From bauxite (Al2O3.2H2O). Bayer's process → pure Al2O3 → Hall-Heroult electrolysis (Al2O3 dissolved in cryolite Na3AlF6, electrolysed at ~1240 K. Cathode: + + 3e- → Al. Anode: C + - → CO/CO2, graphite anode consumed).
Zinc: From ZnS (zinc blende). Froth flotation → roasting (2ZnS + 3O2 → 2ZnO + 2SO2) → reduction with coke (ZnO + C → Zn + CO at 1673 K) → distillation or electrolytic refining.
The key problem-solving concept is applying the Ellingham diagram to predict which reducing agent can reduce a given metal oxide at a specific temperature — the metal whose oxide-formation line lies BELOW can reduce the oxide whose line lies ABOVE.
Key Testable Concept
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