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04-BS-10 · December 2015

Question 8 of 9: Carnot Power Cycle with Air

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

National Exam 04-BS-10, Thermodynamics — December 2015. 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. All state properties (water/steam, air, N₂, CO₂, moist air) were computed from high-accuracy equations of state in place of printed property-table interpolation; every boxed numeric result.

Question 8: Carnot Power Cycle with Air (15 marks)

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. $m=0.5$ kg air. $\eta_{th}=0.50$. Process 1→2 (isothermal expansion): $Q_{12}=40$ kJ. State 1: $P_1=700$ kPa, $V_1=0.12$ m$^3$. Constant properties ($k=1.4$, $R=0.287$ kJ/kg·K, $c_v=0.7175$ kJ/kg·K).

Find. (a) $T_H$, $T_L$ [K]; (b) $V_2$ [m$^3$]; (c) $W$ and $Q$ for each of the four processes [kJ].

V (m³)P (kPa)Q8 — Carnot power cycle, air (P–V)1234
Fig. Q8 — P–V diagram of the Carnot power cycle (1→2 isothermal expansion at $T_H$, 2→3 adiabatic expansion, 3→4 isothermal compression at $T_L$, 4→1 adiabatic compression).

Approach

The Carnot cycle's maximum temperature is fixed directly by the given state-1 conditions via the ideal-gas law; the minimum temperature then follows from the given thermal efficiency ($\eta_{th}=1-T_L/T_H$ for any Carnot engine). The isothermal-expansion heat transfer (equal to its work, since $\Delta U=0$) fixes $V_2$. The two adiabatic legs share the same volume ratio $(T_H/T_L)^{1/(k-1)}$, which fixes $V_3$ and $V_4$; each process's work and heat transfer then follow from the standard ideal-gas isothermal/adiabatic relations.

  1. Maximum temperature (part a). From the ideal-gas law at state 1: $$T_H=\frac{P_1V_1}{mR}=\frac{700\times0.12}{0.5\times0.287}=\boxed{585.37\ \text{K}}.$$
  2. Minimum temperature (part a). Carnot efficiency $\eta_{th}=1-T_L/T_H$: $$T_L=T_H(1-\eta_{th})=585.37\times0.50=\boxed{292.68\ \text{K}}.$$
  3. Volume at end of isothermal expansion (part b). For an ideal gas, isothermal $Q_{12}=W_{12}=mRT_H\ln(V_2/V_1)$: $$V_2=V_1\exp\!\left(\frac{Q_{12}}{mRT_H}\right)=0.12\times\exp\!\left(\frac{40}{0.5\times0.287\times585.37}\right)=\boxed{0.1932\ \text{m}^3}.$$
  4. Adiabatic legs (states 3, 4). Both adiabatic legs share the same volume ratio $(T_H/T_L)^{1/(k-1)}=5.657$ (a general property of the ideal-gas Carnot cycle): $$V_3=V_2\times5.657=1.0929\ \text{m}^3,\qquad V_4=V_1\times5.657=0.6788\ \text{m}^3.$$
  5. Process 1→2: isothermal expansion at $T_H$. $$W_{12}=Q_{12}=\boxed{40.00\ \text{kJ}}.$$
  6. Process 2→3: adiabatic expansion, $T_H\rightarrow T_L$. $Q_{23}=0$; $W_{23}=-\Delta U=mc_v(T_H-T_L)$: $$W_{23}=0.5\times0.7175\times(585.37-292.68)=\boxed{105.00\ \text{kJ}},\qquad Q_{23}=0.$$
  7. Process 3→4: isothermal compression at $T_L$. Heat rejected $Q_L=Q_{12}\,T_L/T_H$ (Carnot ratio): $$Q_{34}=W_{34}=-Q_{12}\frac{T_L}{T_H}=-40\times\frac{292.68}{585.37}=\boxed{-20.00\ \text{kJ}}.$$
  8. Process 4→1: adiabatic compression, $T_L\rightarrow T_H$. $Q_{41}=0$; by symmetry with process 2→3: $$W_{41}=-mc_v(T_H-T_L)=\boxed{-105.00\ \text{kJ}},\qquad Q_{41}=0.$$
  9. Cross-check. $W_{net}=W_{12}+W_{23}+W_{34}+W_{41}=40+105-20-105=20.00$ kJ, and $\eta_{th}=W_{net}/Q_{12}=20.00/40=0.50$ — matches the given 50% exactly.
QuantityResult
(a) $T_H$585.37 K
(a) $T_L$292.68 K
(b) $V_2$0.1932 m³
(c) $W_{12}$, $Q_{12}$ (1→2)40.00 kJ, 40.00 kJ
(c) $W_{23}$, $Q_{23}$ (2→3)105.00 kJ, 0 kJ
(c) $W_{34}$, $Q_{34}$ (3→4)−20.00 kJ, −20.00 kJ
(c) $W_{41}$, $Q_{41}$ (4→1)−105.00 kJ, 0 kJ