This question links the equilibrium and kinetics content of this topic with thermodynamics from elsewhere in the specification. The water-gas shift reaction is used industrially in the production of hydrogen:
CO(g) + H2O(g) ≤> CO2(g) + H2(g)
At a temperature of 600 K, Kc for this equilibrium = 9.00 (no units, since the total number of moles of gas is the same on both sides of the equation). The standard enthalpy change for this reaction is deltaH = -41.0 kJ/mol.
You may use: deltaG = -RT ln(Kc); deltaG = deltaH - T deltaS; R = 8.31 J K-1 mol-1.
(a)Without any calculation, explain why this reaction, although thermodynamically favourable at 600 K (Kc > 1), is carried out industrially in the presence of a catalyst.(2)
(b)Calculate deltaG for this reaction at 600 K, in kJ/mol, to 3 significant figures.(3)
(c)Use your answer to (b), and the value of deltaH given, to calculate deltaS for this reaction, in J K-1 mol-1, to 3 significant figures.(4)
(d)The forward reaction is exothermic. Using Le Chatelier's principle, predict the effect of increasing the temperature above 600 K on the value of Kc, and explain how this is consistent with the (negative) value of deltaS you calculated in (c).(3)
(e)Evaluate whether operating this process at a much higher temperature, such as 900 K instead of 600 K, would be a sensible industrial strategy, considering both the rate at which equilibrium is reached and the equilibrium yield of hydrogen.(2)
(Total for Question 12 is 14 marks)