Chemistry • Year 12 • Module 5 • Lesson 2

Reversibility, Non-Equilibrium Systems & Entropy

Build HSC Band 5–6 extended-response technique on the thermodynamics of reversibility—integrating ΔG°, ΔH, ΔS, entropy of mixing, and real-world non-equilibrium systems.

Master · Extended Response

1. Data – scenario – evaluation — why reactions “don’t go to 100% completion” (Band 5–6)

8 marks   Band 5–6

Scenario. A Year 12 student conducting a research task writes: “I understand that the Haber process reaches equilibrium, but I can’t figure out why the reaction doesn’t just keep going until all the nitrogen and hydrogen have been converted to ammonia. After all, ΔG° is negative, so the forward reaction is spontaneous—shouldn’t it go all the way to products?”

The student then records the following data from a sealed flask experiment at 25°C, monitoring the N2 + 3H2 ⇌ 2NH3 system over time.

Concentration data for a sealed flask at 25°C; ΔG° = −33 kJ/mol. Time in arbitrary units.
Time (AU) [N2] (mol L−1) [H2] (mol L−1) [NH3] (mol L−1) Net change?
01.0003.0000.000Forward rxn dominates
50.7502.2500.500Forward rxn dominates
100.6201.8600.760Slowing
150.5401.6200.920Nearly at equilibrium
200.5301.5900.940Equilibrium reached
300.5301.5900.940No further change

Q1. Write a response that corrects the student’s misunderstanding. In your response you must:

  • Explain what ΔG° tells you (and what it does not tell you) about how far a reaction proceeds.
  • Use the concept of entropy of mixing to explain why a system at intermediate composition has lower free energy than either pure reactants or pure products—even when ΔG° is negative.
  • Use the data in the table to quantify the extent of the reaction at equilibrium and to demonstrate that significant amounts of N2 and H2 remain unreacted.
  • Explain the significance of ΔG = 0 at equilibrium, contrasting it with ΔG° ≠ 0.
  • Apply this reasoning to predict what would be different if ΔG° were −500 kJ/mol rather than −33 kJ/mol.
Plan first: (1) Define what ΔG° tells you (standard thermodynamic driving force, not the same as ΔG along the curve). (2) Entropy of mixing: any intermediate mixture has higher entropy than either pure extreme, so G is lower in the middle. (3) Data: at t=20, 47% of N2 remains. (4) ΔG = 0 at equilibrium vs ΔG° = −33. (5) If ΔG° = −500, the G minimum would shift almost entirely to the products side.

2. Evaluate a thermodynamics claim — combustion, entropy, and irreversibility (Band 5–6)

7 marks   Band 5–6

“The reason combustion of petrol in a car engine is irreversible is simple: the fuel burns in an open system with excess air, so equilibrium can never be established. If you could put the combustion products back in a perfectly sealed flask, the system would reach equilibrium and some petrol and oxygen would reform from the carbon dioxide and water vapour.”

— Attributed to a popular chemistry blog, 2023.

Q2. Evaluate this claim. Identify which parts are chemically defensible and which are incorrect or misleading. Reformulate the claim into a chemically and thermodynamically defensible statement that accurately explains why combustion is irreversible. In your response you must:

Plan first: (1) What determines irreversibility? ΔG magnitude, not system type. (2) Combustion: ΔH << 0 and ΔS > 0, so both terms make ΔG very negative—“doubly irreversible”. (3) Sealed flask: even in a sealed flask, ΔG° = −hundreds of kJ/mol means Keq is astronomically large—essentially no petrol would reform. (4) Australian examples: Black Summer bushfire combustion (irreversible) vs N2O4 ⇌ 2NO2 (reversible).
Answers — Do not peek before attempting

Q1 — Sample Band 6 response (8 marks), annotated

The student’s misunderstanding arises from conflating ΔG° with ΔG (the actual free energy change at a specific composition). ΔG° = −33 kJ/mol tells us that, under standard conditions (1 mol L⊃−¹ of all species at 25°C), the forward reaction is spontaneous—but it does not tell us the reaction will go to completion. ΔG° quantifies the thermodynamic driving force from the standard state, not from any mixture of reactants and products. [1 — correctly distinguishes ΔG° from ΔG]

The reason the system does not go to completion is the concept of entropy of mixing. Any mixture of reactants and products has higher entropy than either pure extreme, because mixing increases disorder. This means the Gibbs free energy of an intermediate composition is lower than both pure reactants and pure products—the system always “falls into” an intermediate minimum free energy state rather than converting completely to products. This is the thermodynamic reason all reactions with moderate |ΔG°| reach equilibrium with both species present. [2 — entropy of mixing explanation, 1 for concept and 1 for linking to lower G at intermediate composition]

The data confirm this: at equilibrium (t = 20–30), [N2] = 0.530 mol L−1—53% of the initial 1.000 mol L−1 N2 remains unreacted. Similarly, [H2] = 1.590 mol L−1 (53% remains). Only 0.940 mol L−1 NH3 has formed from a possible 2.000 mol L−1—a 47% conversion. Significant amounts of both reactants are present at equilibrium. [1 — correct use of data to quantify unreacted N2/H2]

At equilibrium, ΔG = 0 (not ΔG°). This is the crucial distinction. ΔG = 0 means the free energy of the system is at its minimum—neither the forward nor the reverse reaction has a thermodynamic driving force at that composition. ΔG° = −33 kJ/mol is the driving force from the standard state (1 mol L−1 of all species) towards equilibrium; it is non-zero because the standard state is not the equilibrium state. Once the system reaches equilibrium, ΔG = 0 and no further net change occurs in either direction. [2 — ΔG = 0 at equilibrium and its distinction from ΔG°]

If ΔG° were −500 kJ/mol rather than −33 kJ/mol, the Gibbs free energy minimum would shift almost entirely to the products side. The entropy of mixing contribution would be negligible compared to the enormous thermodynamic preference for products. Essentially all reactants would be converted—the reaction would behave as irreversible, and the data table would show [N2] and [H2] approaching zero at equilibrium. [1 — prediction applied correctly]

Marking criteria.

  • 1 mark — Correctly states that ΔG° quantifies the standard-state driving force and does not predict completion; distinguishes ΔG° from ΔG.
  • 1 mark — Names and correctly explains the entropy of mixing concept.
  • 1 mark — Explains that intermediate mixtures have higher entropy (lower G) than either pure extreme, so the G minimum lies at an intermediate composition for moderate ΔG°.
  • 1 mark — Uses the data table to quantify unreacted reactants at equilibrium (e.g. 53% of N2 remains, 47% conversion of NH3).
  • 1 mark — States ΔG = 0 at equilibrium and explains this as the minimum free energy state with no thermodynamic driving force.
  • 1 mark — Correctly distinguishes ΔG = 0 (equilibrium condition) from ΔG° ≠ 0 (standard-state driving force).
  • 1 mark — Predicts (correctly) that ΔG° = −500 kJ/mol would shift the equilibrium almost entirely to products, approaching irreversible behaviour.
  • 1 mark (bonus/Band 6 discriminator) — Explicitly connects all three points: entropy of mixing + magnitude of ΔG° + meaning of ΔG = 0, in a coherent argument that fully corrects the student’s misunderstanding without oversimplification.

Q2 — Sample Band 6 response (7 marks), annotated

The blog claim contains one defensible observation but is fundamentally incorrect in its core argument.

Defensible element: It is true that combustion of petrol in a car engine occurs in an open system (exhaust gases escape), and that open systems cannot reach closed-system dynamic equilibrium. [1 — concedes one correct element]

What is incorrect: The claim implies that the open system is the reason combustion is irreversible—suggesting that in a sealed flask, equilibrium with measurable petrol would reform. This is thermodynamically wrong. Irreversibility is determined by the magnitude of ΔG, not by the system type. [1 — correctly identifies the flaw in logic]

Using ΔG = ΔH − TΔS for combustion of octane (a major petrol component, C8H18): ΔH ≈ −5471 kJ/mol (strongly exothermic; products CO2 and H2O are far more thermodynamically stable than octane and O2). ΔS is large and positive (solid/liquid octane and gas O2 → CO2(g) + H2O(g); large increase in gas moles and disorder). Therefore ΔG = ΔH − TΔS is the sum of a very large negative enthalpy term and an additional negative −TΔS term—both terms drive ΔG to be extremely large and negative. This makes combustion “doubly irreversible”: the thermodynamic preference for products is reinforced by both enthalpy and entropy simultaneously. [2 — 1 for correct signs and 1 for “doubly irreversible” argument]

The sealed-flask scenario: Even in a perfectly sealed flask, the equilibrium constant Keq would be astronomically large (related to ΔG° by the equation ΔG° = −RT ln K; for ΔG° ≈ −5000 kJ/mol, Keq ≈ 10875). The amount of petrol that would reform at equilibrium is so vanishingly small as to be physically meaningless—no measurable petrol would ever appear. The claim that “equilibrium with reformed petrol” would exist in a sealed flask is therefore incorrect. [1 — sealed flask reasoning with Keq argument]

Australian examples: Combustion of eucalypt oils during a Black Summer bushfire in south-east Australia (e.g. the 2019–2020 fires burning more than 18 million hectares) has ΔG ≈ −thousands of kJ/mol—irreversible; the burnt landscape cannot spontaneously regenerate by reversing the reaction. In contrast, N2O4(g) ⇌ 2NO2(g) (the brown-gas equilibrium visible in sealed ampoules of nitrogen dioxide) has ΔG° = +4.7 kJ/mol at 25°C—a small value indicating a genuinely reversible equilibrium where both colourless N2O4 and brown NO2 are measurably present. [1 — named Australian irreversible example and named reversible example with thermodynamic contrast]

Defensible reformulation: “Combustion of petrol is irreversible not primarily because it occurs in an open system, but because both ΔH and ΔS make ΔG extremely negative. The free energy minimum lies almost entirely at the products side, so the reverse reaction (reformation of petrol from CO2 and H2O) has a ΔG of thousands of kJ/mol in the positive direction—essentially impossible under normal conditions regardless of system type.” [1 — chemically and thermodynamically defensible reformulation]

Marking criteria.

  • 1 mark — Identifies the one defensible element (open system cannot reach closed-system dynamic equilibrium; this part is correct in itself).
  • 1 mark — Correctly identifies the flaw: the claim implies system type determines irreversibility; in fact it is the magnitude of ΔG.
  • 1 mark — Correctly applies ΔG = ΔH − TΔS to combustion: states ΔH << 0 and ΔS > 0, so both terms make ΔG very large and negative.
  • 1 mark — Makes the “doubly irreversible” argument: both ΔH and TΔS reinforce irreversibility simultaneously (unlike reactions where only one term favours the forward direction).
  • 1 mark — Addresses the sealed-flask assertion: even in a sealed flask, Keq is astronomically large so no measurable petrol would reform; the claim is incorrect.
  • 1 mark — Names at least one real-world Australian irreversible combustion example (e.g. bushfire) and one reversible reaction (e.g. N2O4/NO2, Haber process, H2/I2/HI) and uses both to illustrate the thermodynamic spectrum.
  • 1 mark — Produces a chemically and thermodynamically defensible reformulation of the claim that correctly centres irreversibility on the magnitude of ΔG rather than system type.