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Gibbs free energy brings together everything we have covered in this course — enthalpy and entropy — into a single quantity that tells us whether a reaction is thermodynamically feasible. This is one of the most important concepts in chemistry, and a frequent topic in A-Level exam questions. This lesson covers the Gibbs equation, the four cases of feasibility, finding transition temperatures, and worked calculations across a range of contexts.
ΔG = ΔH − TΔS
where:
A reaction is thermodynamically feasible (spontaneous) when ΔG < 0 (negative).
A reaction is not feasible when ΔG > 0 (positive).
When ΔG = 0, the system is at equilibrium.
Critical reminder: ΔS is usually given in J K⁻¹ mol⁻¹. You MUST divide by 1000 to convert to kJ K⁻¹ mol⁻¹ before substituting into the equation. Forgetting this conversion is one of the most common errors in exam questions.
The signs of ΔH and ΔS together determine whether a reaction is feasible and how temperature affects feasibility.
| Case | ΔH | ΔS | ΔG = ΔH − TΔS | Feasibility |
|---|---|---|---|---|
| 1 | Negative | Positive | Always negative | Feasible at all temperatures |
| 2 | Positive | Negative | Always positive | Never feasible |
| 3 | Negative | Negative | Depends on T | Feasible at low temperatures |
| 4 | Positive | Positive | Depends on T | Feasible at high temperatures |
ΔG = (negative) − T(positive) = negative − positive = always negative
The reaction is feasible at all temperatures. Both the enthalpy and entropy changes favour the reaction.
Example: 2H₂O₂(l) → 2H₂O(l) + O₂(g), ΔH = −196 kJ mol⁻¹, ΔS = +125.6 J K⁻¹ mol⁻¹
ΔG = (positive) − T(negative) = positive + positive = always positive
The reaction is never feasible at any temperature. Both terms oppose the reaction.
Example: 3O₂(g) → 2O₃(g). This reaction has positive ΔH and negative ΔS.
ΔG = (negative) − T(negative) = negative + positive
At low temperatures, the negative ΔH dominates and ΔG is negative → feasible. At high temperatures, the TΔS term becomes large enough to make ΔG positive → not feasible.
Example: N₂(g) + 3H₂(g) → 2NH₃(g), ΔH = −92 kJ mol⁻¹, ΔS = −198.8 J K⁻¹ mol⁻¹
ΔG = (positive) − T(positive) = positive − positive
At low temperatures, the positive ΔH dominates and ΔG is positive → not feasible. At high temperatures, the TΔS term exceeds ΔH, making ΔG negative → feasible.
Example: CaCO₃(s) → CaO(s) + CO₂(g), ΔH = +178 kJ mol⁻¹, ΔS = +160.4 J K⁻¹ mol⁻¹
graph LR
subgraph "Case 3: ΔH < 0, ΔS < 0"
A1["Low T: feasible"] --> A2["High T: not feasible"]
end
subgraph "Case 4: ΔH > 0, ΔS > 0"
B1["Low T: not feasible"] --> B2["High T: feasible"]
end
For Cases 3 and 4, there is a specific temperature at which the reaction switches between feasible and not feasible. This is found by setting ΔG = 0:
ΔG = 0 when ΔH = TΔS
Therefore: T = ΔH / ΔS
(Use consistent units: ΔH in kJ mol⁻¹ and ΔS in kJ K⁻¹ mol⁻¹, or both in J.)
CaCO₃(s) → CaO(s) + CO₂(g)
ΔH = +178 kJ mol⁻¹, ΔS = +160.4 J K⁻¹ mol⁻¹ = +0.1604 kJ K⁻¹ mol⁻¹
T = ΔH / ΔS = 178 / 0.1604 = 1110 K (approximately 837 °C)
Below this temperature, ΔG > 0 and the reaction is not feasible. Above this temperature, ΔG < 0 and the reaction is feasible.
In practice, limestone (CaCO₃) is heated to about 900–1000 °C in a lime kiln to produce quicklime (CaO), consistent with our calculation.
N₂(g) + 3H₂(g) → 2NH₃(g)
ΔH = −92 kJ mol⁻¹, ΔS = −198.8 J K⁻¹ mol⁻¹ = −0.1988 kJ K⁻¹ mol⁻¹
T = ΔH / ΔS = −92 / −0.1988 = 463 K (approximately 190 °C)
Below 463 K, ΔG < 0 — the reaction is feasible. Above 463 K, ΔG > 0 — the reaction is not feasible.
Yet the Haber process operates at 400–500 °C. Why? Because thermodynamic feasibility (ΔG < 0) does not guarantee a useful rate. At low temperatures the rate is too slow. The high temperature is used with a catalyst to achieve a reasonable rate, accepting a lower equilibrium yield.
C₂H₅OH(l) + 3O₂(g) → 2CO₂(g) + 3H₂O(l)
ΔH = −1367 kJ mol⁻¹, ΔS = −138.8 J K⁻¹ mol⁻¹ = −0.1388 kJ K⁻¹ mol⁻¹
ΔG = ΔH − TΔS = (−1367) − (298)(−0.1388) = −1367 + 41.4 = −1325.6 kJ mol⁻¹
ΔG is very negative — the reaction is strongly feasible. The small positive TΔS term barely affects the large exothermic enthalpy change.
NH₄NO₃(s) → NH₄⁺(aq) + NO₃⁻(aq)
ΔH = +25.7 kJ mol⁻¹, ΔS = +108.7 J K⁻¹ mol⁻¹ = +0.1087 kJ K⁻¹ mol⁻¹
ΔG = 25.7 − (298)(0.1087) = 25.7 − 32.4 = −6.7 kJ mol⁻¹
ΔG is negative despite ΔH being positive. The entropy increase drives the reaction at room temperature. This is why ammonium nitrate feels cold when it dissolves — the process is endothermic but thermodynamically feasible.
Fe₂O₃(s) + 3C(s) → 2Fe(s) + 3CO(g)
ΔH = +490 kJ mol⁻¹, ΔS = +543 J K⁻¹ mol⁻¹ = +0.543 kJ K⁻¹ mol⁻¹
T = ΔH / ΔS = 490 / 0.543 = 902 K (approximately 629 °C)
Above about 900 K, the entropy term dominates and the reduction of iron oxide by carbon becomes feasible. In a blast furnace, temperatures exceed 1500 °C, well above this threshold.
ΔG tells us whether a reaction can happen (thermodynamic feasibility), not whether it will happen quickly (kinetics):
| Mistake | Correction |
|---|---|
| Not converting ΔS from J to kJ | Divide ΔS by 1000 before using in ΔG = ΔH − TΔS |
| Using °C instead of K for temperature | Always convert: T(K) = T(°C) + 273 |
| Saying ΔG < 0 means the reaction is fast | ΔG tells us about feasibility, not rate |
| Confusing the transition temperature with the actual operating temperature | T = ΔH/ΔS gives the boundary; industrial processes may operate well above or below |
| Forgetting that ΔG = 0 at equilibrium, not at the transition temperature only | At the transition temperature, the system is at the boundary between feasible and not feasible |
Edexcel 9CH0 specification Topic 13 introduces Gibbs free energy via ΔG° = ΔH° − TΔS° as the predictor of thermodynamic spontaneity at constant temperature and pressure (refer to the official specification document for exact wording). Candidates must compute ΔG°, predict whether a reaction is spontaneous (ΔG° < 0), and determine the temperature at which ΔG° = 0 — the "spontaneity threshold" above which an entropy-driven endothermic reaction becomes spontaneous, or below which an entropy-disfavoured exothermic reaction remains spontaneous. Gibbs questions appear on Paper 1 as multi-step calculations and on Paper 3 as synoptic items connecting thermodynamics to equilibrium constants (ΔG° = −RT ln K). Unit handling (J vs kJ; J K⁻¹ vs kJ K⁻¹) is critical and frequently tested.
Question (8 marks):
For the thermal decomposition of magnesium carbonate: MgCO₃(s) → MgO(s) + CO₂(g).
ΔH° = +117 kJ mol⁻¹; ΔS° = +175 J K⁻¹ mol⁻¹.
(a) Calculate ΔG° at 298 K. (2) (b) Determine the temperature above which the reaction becomes thermodynamically spontaneous. (3) (c) Compare your answer to (b) with the experimental decomposition temperature of MgCO₃ (~350 °C ≈ 623 K) and account for any discrepancy. (3)
Solution with mark scheme:
(a) Convert ΔS° to kJ: ΔS° = 0.175 kJ K⁻¹ mol⁻¹.
ΔG° = ΔH° − TΔS° = 117 − 298 × 0.175 = 117 − 52.15 = +64.9 kJ mol⁻¹.
M1 — correct unit conversion or matching units. A1 — correct value with sign.
(b) Threshold: ΔG° = 0 ⟹ T = ΔH°/ΔS°.
T = 117 / 0.175 = 669 K (≈ 396 °C).
M1 — recognise ΔG° = 0 condition. M1 — substitute and divide. A1 — answer with units.
(c) B1 — calculated threshold (669 K) is higher than the observed decomposition temperature (623 K), a difference of ~46 K.
B1 — possible reasons: (i) the reaction does not need to be in equilibrium for decomposition to proceed if CO₂ is continuously removed (Le Chatelier); (ii) ΔH° and ΔS° have temperature dependence (assumed constant in the calculation); (iii) experimental "decomposition temperature" is the temperature of visible decomposition, not strict ΔG° = 0.
B1 — the small (~7%) discrepancy validates the thermodynamic prediction; the framework is robust within typical experimental uncertainties.
Total: 8 marks (M3 A2 B3).
Question (6 marks):
Hydrogen iodide synthesis: H₂(g) + I₂(g) ⇌ 2HI(g). ΔH° = −10 kJ mol⁻¹; ΔS° = +22 J K⁻¹ mol⁻¹.
(a) Show that ΔG° at 298 K is negative and calculate its value. (2) (b) Use ΔG° = −RT ln K to estimate the equilibrium constant K at 298 K. (R = 8.31 J K⁻¹ mol⁻¹) (3) (c) Predict (with reasoning) whether K increases or decreases at 600 K. (1)
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