Equilibria
Le Chatelier, Kc and Kp
Le Chatelier's principle
- Position shifts to oppose a change. Raise T → shifts in the endothermic direction. Raise p → shifts to fewer gas moles. Catalyst → no shift, equilibrium reached faster.
- Haber process (N₂ + 3H₂ ⇌ 2NH₃, ΔH = −92 kJ mol⁻¹): compromise 400–450 °C, ~200 atm, iron catalyst — low T favours yield but is too slow.
Equilibrium constant
Kc = [C]c[D]d / [A]a[B]b- K changes only with temperature. For an exothermic reaction, raising T decreases K.
- Concentration/pressure changes move the position but K is unchanged.
- Kp uses partial pressures: p(X) = mole fraction × total pressure.
3.1.6.2Kc from equilibrium data — the ICE routine
- Initial: 1.00 / 1.00 / 0 · Change: −0.80 / −0.80 / +1.60 · Equilibrium: 0.20 / 0.20 / 1.60 mol
- Kc = [HI]² ÷ ([H₂][I₂]) = 1.60² ÷ (0.20 × 0.20) = 64 (no units — concentrations cancel).
3.1.10Kp — the same idea with pressures
- Mole fraction x = moles of gas ÷ total moles; partial pressure p = x × P(total); Kp built exactly like Kc but with partial pressures of gases only.
- Solids and pure liquids never appear in Kp expressions.
- Like Kc, Kp changes with temperature only — pressure shifts the position, not the constant.
3.1.6.3The three industrial equilibria
| Process | Reaction | Catalyst | Conditions | Why the compromise |
|---|---|---|---|---|
| Haber | N₂ + 3H₂ ⇌ 2NH₃ (ΔH −92) | Fe | 400–450 °C, ~200 atm | low T = better yield but too slow; ~15% per pass, gases recycled |
| Contact | 2SO₂ + O₂ ⇌ 2SO₃ | V₂O₅ | ~450 °C, ~2 atm | yield already ~99.5% near atmospheric pressure — high p not worth it |
| Ethanol | C₂H₄ + H₂O ⇌ C₂H₅OH | H₃PO₄ | 300 °C, 60–70 atm | ~5% per pass; unreacted ethene recycled |
Extended🎓 Beyond the standard course
- The reaction quotient Q is Kc's expression evaluated with current concentrations. Q < K → forward shift; Q > K → reverse; Q = K → equilibrium. This single comparison replaces all hand-waving about "position".
- van 't Hoff: a plot of ln K against 1/T is linear with gradient −ΔH°/R — the quantitative version of "heating an exothermic equilibrium lowers K", and the exact mirror of Arrhenius for kinetics.
- Why solids never appear in K: their concentration (density ÷ molar mass) is fixed — formally, their activity is 1. CaCO₃(s) ⇌ CaO(s) + CO₂(g) reduces to Kp = p(CO₂): one gas controls the whole equilibrium.
- Small-K approximation: when K is tiny, "x is negligible against c" turns quadratics into one-liners — the same 5% rule you use for weak acids.
Deep dive📚 The rest of the chapter, in full
Kc from scratch: the ICE method
Kc units: build them from the expression each time. For N₂ + 3H₂ ⇌ 2NH₃, Kc = [NH₃]²/([N₂][H₂]³) has units (mol dm⁻³)² ÷ (mol dm⁻³)⁴ = mol⁻² dm⁶.
The golden rule of K
Only temperature changes K. Concentration, pressure and catalysts shift the position of equilibrium (or just the speed of reaching it) while K stays fixed. For an exothermic forward reaction, raising T decreases K; for endothermic, K increases. This one sentence — "Kc is unchanged because temperature is constant" — earns a mark in almost every equilibrium question about adding reagent or compressing the mixture.
Le Chatelier, systematically
| Change | Position shifts… | K |
|---|---|---|
| Add a reactant | Right (to remove it) | Unchanged |
| Raise pressure (gases) | To the side with fewer moles of gas | Unchanged |
| Raise temperature | In the endothermic direction | Changes |
| Catalyst | No shift — equilibrium reached faster | Unchanged |
Industrial compromises
Haber (N₂ + 3H₂ ⇌ 2NH₃, ΔH = −92 kJ mol⁻¹): low T favours yield but is slow; high P favours yield but is expensive and hazardous. Compromise: ~450 °C, ~200 atm, iron catalyst, and ammonia is liquefied out to pull the equilibrium right. Contact (2SO₂ + O₂ ⇌ 2SO₃, exothermic): ~450 °C, ~2 atm (already 99%+ conversion, so high pressure is not worth paying for), V₂O₅ catalyst. Arguments about conditions = rate vs yield vs cost, always all three.
Kp (Year 2)
For gases use partial pressures: p(X) = mole fraction × total pressure. Kp for N₂O₄ ⇌ 2NO₂ is p(NO₂)²/p(N₂O₄), units built the same way (here: kPa). Solids and pure liquids never appear in Kp or heterogeneous Kc expressions — their "concentration" is constant. Only temperature changes Kp; compressing the mixture shifts position until the same Kp is restored.
Mastery vault🏛 Every remaining spec point, banked
Kc when the volume refuses to cancel
Kp from first principles
- Partial pressure = mole fraction × total pressure; the partial pressures must sum to the total (use this as a check).
- Raising total pressure does not change Kp — the system shifts (here toward PCl₅) until the same Kp is restored with new partial pressures.
- Heterogeneous equilibria omit solids and pure liquids: for CaCO₃(s) ⇌ CaO(s) + CO₂(g), Kp = p(CO₂) alone — at a given temperature the CO₂ pressure above limestone is fixed no matter how much solid is present.
Interpreting K values
K ≫ 1: products dominate; K ≪ 1: barely reacts; K ≈ 1: comparable amounts. K says nothing about SPEED — H₂ + O₂ has a colossal K at 298 K yet a match is needed (kinetic barrier). Comparing K at two temperatures identifies ΔH's sign: K falling as T rises → forward reaction exothermic.
Ethanol two ways — the industrial comparison
| Hydration of ethene | Fermentation | |
|---|---|---|
| Equation | C₂H₄ + H₂O ⇌ C₂H₅OH | C₆H₁₂O₆ → 2C₂H₅OH + 2CO₂ |
| Conditions | 300 °C, 60–70 atm, H₃PO₄ catalyst | ~35 °C, yeast, anaerobic |
| Rate / purity | Fast, essentially pure product | Slow, dilute — needs fractional distillation |
| Feedstock | Finite (crude oil) | Renewable (sugars) |
| Process | Continuous, low labour | Batch, higher labour |
Unreacted ethene is recycled over the catalyst — the standard fix when a compromise position leaves conversion low (same trick as the Haber loop). "Carbon-neutral" claims for fermentation ethanol fail once farming, transport and distillation energy are counted — a routine evaluation point.
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