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)
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.
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).
Quantity
Result
(a) $\Delta s$
−0.34461 kJ/kg·K
(b) Adiabatic?
No — would require $s_{gen}<0$, violating the 2nd law