A synthetic chemist is modifying the combustion of a generic hydrocarbon fuel, CnH2n+2(g), by partially substituting the fuel with an oxygenated additive, CnH2nO(g), to attain a near-zero enthalpy change for the overall combustion mixture. Assume complete combustion to CO2(g) and H2O(l) and neglect any phase changes other than the formation of liquid water.
Let the mole fraction of the oxygenated additive in the fuel blend be f (0 ≤ f ≤ 1). The blend composition is therefore (1−f) mol CnH2n+2 and f mol CnH2nO.
Average bond enthalpies (representative, in kJmol−1):
C–H 413 C–C 348 C–O 358 C=O (in CO2) 799 O=O 498 O–H 463
Additional information:
• Combustion of CnH2n+2(g): CnH2n+2+(3n+21)O2→nCO2+(n+1)H2O(l)ΔH1∘ (depends on n)
• Combustion of CnH2nO(g): CnH2nO+23nO2→nCO2+nH2O(l)ΔH2∘ (depends on n)
• For this question, treat ΔH1∘ and ΔH2∘ as unknown expressions derived solely from average bond energies and show them symbolically in your work.
(1) Part 1: a. Derive an expression for the overall standard enthalpy change, ΔHblend(f), for complete combustion of 1 mole of the fuel blend as a function of the mole fraction f.
(2) Part 2: b. Determine the value of f that makes ΔHblend(f) exactly zero. Express your answer algebraically in terms of n and any constants that appear in your expression.
(3) Part 3: c. For the specific case n=8 (octane family), evaluate numerically the value of f using the average bond enthalpies supplied. Show all intermediate steps.
(4) Part 4: d. Critically assess whether the calculated mole fraction f is practically achievable in a real combustion engine, citing at least two operational or chemical factors that could deviate from the idealized bond-enthalpy model used.