Here, we are given
Δf G° (NH3 ) = – 16.8 kJ mol–1
Δf G° (NO) = + 86.7 kJ mol–1
Δf G° (H2O) = – 237.2 kJ mol–1
∴ Δf G° = ∑f G° (Products) ∑ Δf G° (Reactants)
=[14 × Δf G° (NO) + 6 × Δf G°(H2O)] – [4 × Δf G° (NH3 ) + 5 × Δf G° (O2 )]
= [4 × (86.7) + 6 × (–237.2)] – [4 × (– 16.8) + 5 × 0] = – 1009.2 kJ
Since Δf G° is negative, the process is feasible.