Part of PC-06 — Equilibrium: Chemical & Ionic

Application Note — Industrial and Real-World Applications

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1. Haber Process (Ammonia Synthesis)

$N_{2}$(g) + $3H_{2}$(g) --[Fe catalyst, 400-500°C, 150-200 atm]--> $2NH_{3}$(g) ΔH\Delta H = −92 kJ/mol (exothermic)

  • Le Chatelier optimisation: High pressure shifts toward fewer gas moles (Δn\Delta n = −2) → favours NH3NH_{3}
  • Temperature compromise: Low T favours NH3NH_{3} (exothermic) but reaction is too slow; 400–500°C used with catalyst
  • Catalyst: Fe with K2OK_{2}O and Al2O3Al_{2}O_{3} promoters; does not change K but speeds equilibration

2. Blood Buffer System

  • Blood pH = 7.35–7.45 (slightly basic)
  • Carbonate buffer: CO2CO_{2}/HCO3HCO_{3}^{-} system; pKa ≈ 6.1
  • Henderson-Hasselbalch: pH=6.1+log[HCO3][CO2]pH = 6.1 + \log\frac{[\text{HCO}_3^-]}{[\text{CO}_2]} ≈ 6.1 + log(20/1) ≈ 7.4
  • Acidosis: pH < 7.35; Alkalosis: pH > 7.45

3. Selective Precipitation in Qualitative Analysis

  • Adding H2SH_{2}S in acidic medium selectively precipitates Group II cations (low Ksp sulfides)
  • Adding H2SH_{2}S in basic medium precipitates Group III cations (higher Ksp sulfides)
  • Exploits Ksp differences and common ion effect (H+H^{+} concentration controls S2S^{2-} concentration)

4. Antacids

  • Mg(OH){2} and Al(OH){3} in antacids neutralise excess HCl in stomach (Arrhenius base concept)
  • Mg(OH)_{2} + 2HCl → MgCl2MgCl_{2} + 2H2O2H_{2}O
  • Calcium carbonate (SMILES: OC(=O)[O-].[Ca+2]): CaCO3CaCO_{3} + 2HCl → CaCl2CaCl_{2} + H2OH_{2}O + CO2CO_{2}

5. Solubility in Water Treatment

  • Lime softening: Ca2+Ca^{2+} + CO32CO_{3}^{2-}CaCO3CaCO_{3}↓ (ionic product exceeds Ksp)
  • Fluoridation controlled by CaF2CaF_{2} Ksp to maintain safe [FF^{-}] levels

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