04-BS-10 · December 2016
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exam 04-BS-10, Thermodynamics — December 2016. 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, interpolation not required). 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. All state properties (water/steam, R-134a, air, N₂, CO₂) were computed from high-accuracy equations of state in place of printed property-table interpolation; every boxed numeric result.
Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.
Given. Inlet: $P_1=300$ kPa, $T_1=52\ ^\circ$C. Exit: $P_2=100$ kPa, $T_2=12\ ^\circ$C. $\dot m=10$ kg/s. Adiabatic, $\Delta$KE $=\Delta$PE $=0$.
Find. $\dot W$ [kW]; reversibility; $\eta_t$ if irreversible.
The actual power follows directly from the steady-flow energy balance using the given inlet/exit enthalpies. Reversibility for an adiabatic process is judged purely by the entropy change: compute $s_1$ and $s_2$ from the given $(T,P)$ pairs via the variable-cp air relation and compare. If $s_2>s_1$, the process is irreversible, and the isentropic efficiency follows from a separate isentropic-exit calculation at the same exit pressure.
| Quantity | Result |
|---|---|
| $\dot W$ | 402.65 kW |
| Reversible? | No ($s_{gen}=0.1832$ kJ/kg·K $>0$) |
| $\eta_t$ | 0.4575 (45.8%) |