Question 8 of 9: Ideal Otto Cycle — Variable Specific Heats
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exam 04-BS-10, Thermodynamics — December 2014. 3 hours, Closed-Book Exam
(approved calculator and one double-sided 8.5x11-inch aid sheet permitted; property tables and
charts supplied in an appendix). Part A: answer 2 of Questions 1-3 (20 marks each). Part B: answer
4 of Questions 4-9 (15 marks each), for a 100-mark paper. Only the first two Part-A and first four
Part-B questions as they appear in the answer book are marked. All nine questions (Part A complete,
Part B complete) are solved below for completeness.
Reference texts: Cengel & Boles, Thermodynamics: An Engineering
Approach, 8th ed.; Moran, Shapiro, Boettner & Bailey, Fundamentals of Engineering
Thermodynamics, 8th ed. State properties for the real-fluid questions (R-134a, water/steam,
moist air, air) were computed from high-accuracy equations of state in place of printed property-table
interpolation. Question 5 is the exception: it directs that the mixture be treated as an ideal gas,
so its N₂ and O₂ enthalpies are taken from the ideal-gas tables supplied with the paper.
Question 8: Ideal Otto Cycle — Variable Specific Heats (15 marks)
Given. Compression ratio $r=8$. $T_1=310$ K (start of compression, cycle
minimum), $T_3=1600$ K (end of constant-volume heat addition, cycle maximum). Air-standard,
variable specific heats.
Fig. Q8 — P–v state points for the ideal Otto cycle (1→2
isentropic compression, 2→3 constant-volume heat addition, 3→4 isentropic expansion,
4→1 constant-volume heat rejection).
Approach
Solve each isentropic leg (compression 1→2, expansion 3→4) by root-finding on
temperature against the fixed volume ratio $r=8$, using variable-specific-heat air properties rather
than a constant-$k$ shortcut. Internal energies at all four states then give the heat-addition,
heat-rejection, net work and thermal efficiency directly.
Isentropic compression (1→2), $v_1/v_2=r=8$. Solving
$s^\circ(T_2)-s^\circ(T_1)=R\ln[(T_2/T_1)(v_1/v_2)]=0$ for $T_2$: $T_2=692.86$ K. Internal energies:
$u_1=347.40$ kJ/kg, $u_2=633.08$ kJ/kg.
Isentropic expansion (3→4), $v_4/v_3=r=8$. Same root-find with the
expansion-leg volume ratio: $T_4=809.88$ K. Internal energies: $u_3=1424.59$ kJ/kg (at the given
$T_3=1600$ K), $u_4=726.72$ kJ/kg.
Heat rejection, constant volume 4→1, and net work (part b).
$$q_{out}=u_4-u_1=726.72-347.40=379.32\ \text{kJ/kg}.$$
$$w_{net}=q_{in}-q_{out}=791.50-379.32=\boxed{412.18\ \text{kJ/kg}}.$$