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04-BS-10 · December 2014

Question 6 of 9: R-134a — Entropy Change and Feasibility of an Adiabatic Process

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 6: R-134a — Entropy Change and Feasibility of an Adiabatic Process (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. State 1: $P_1=700$ kPa, $x_1=0.50$. State 2: $T_2=16\ ^\circ$C, saturated liquid ($x_2=0$). $m=1$ kg.

Find. (a) $\Delta s$ [kJ/kg·K]; (b) feasibility of an adiabatic path.

Approach

Look up the entropy at each named state directly and take the difference; for part (b), recognize that a closed system undergoing an adiabatic process obeys $\Delta s=s_{gen}\ge0$, so any process with $\Delta s<0$ is impossible without heat removal.

  1. State entropies. $s_1=1.42182$ kJ/kg·K (700 kPa, $x=0.50$). $s_2=1.07721$ kJ/kg·K (saturated liquid, 16°C).
  2. Entropy change (part a). $$\Delta s=s_2-s_1=1.07721-1.42182=\boxed{-0.34461\ \text{kJ/kg}\cdot\text{K}}.$$
  3. Adiabatic feasibility (part b). For a closed system with no heat transfer, $\Delta s=s_{gen}$, and the second law requires $s_{gen}\ge0$. Since $\Delta s=-0.34461$ kJ/kg·K $<0$, this process cannot be accomplished adiabatically — it requires heat to be removed from the refrigerant as it condenses and cools, which is exactly what would be expected physically (going from a warm two-phase mixture to a cooler saturated liquid).
QuantityResult
(a) $\Delta s$−0.34461 kJ/kg·K
(b) Adiabatic?No — would require $s_{gen}<0$, violating the 2nd law