Question 9 of 9: Uncontrolled Expansion into an Evacuated Compartment
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exam 04-BS-10, Thermodynamics — May 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,
moist air) were computed from high-accuracy equations of state in place of printed property-table interpolation; every boxed numeric result.
Question 9: Uncontrolled Expansion into an Evacuated Compartment (15 marks)
Given. Insulated (adiabatic), rigid, two-compartment vessel. Initial: steam at
$P_1=1.0$ MPa, $T_1=500\ ^\circ$C fills compartment A; compartment B is evacuated. Valve opens,
steam expands to fill the whole vessel at $P_2=0.1$ MPa.
The whole two-compartment vessel is rigid and insulated, so across the entire (fixed-mass)
system there is no heat transfer and no boundary work — the total internal energy is
conserved, $u_2=u_1$ (this is not a throttling process with $h_2=h_1$; that relation
applies to steady flow through a valve from an external line, not to an uncontrolled expansion
inside a single closed, insulated vessel). The final temperature is then whatever satisfies
$u(P_2,T_2)=u_1$ at the given final pressure. The fraction of the vessel initially occupied by the
steam follows from the specific volumes ($V\propto v$ at fixed mass), and the entropy produced is
simply $s_2-s_1$ since this isolated system exchanges no entropy with its surroundings.
Final temperature (part a). Energy conservation for the isolated,
insulated, rigid vessel (no work crosses its outer boundary, no heat transfer):
$$u_2=u_1=3124.99\ \text{kJ/kg}.$$
Solving for $T_2$ at $P_2=0.1$ MPa such that $u(P_2,T_2)=3124.99$ kJ/kg:
$$T_2=\boxed{495.69\ ^\circ\text{C}}\quad(v_2=3.5456\ \text{m}^3/\text{kg},\ s_2=8.8242\ \text{kJ/kg}\cdot\text{K}).$$
Vessel-fraction initially occupied by steam (part b). Since the total mass is
fixed and the vessel is rigid, $V\propto v$ at each state, so the initial fraction is simply the
ratio of specific volumes:
$$\frac{V_A}{V_{total}}=\frac{v_1}{v_2}=\frac{0.35411}{3.5456}=\boxed{0.0999\ (10.0\%)}.$$
Entropy generation (part c). The combined vessel is isolated (no mass, heat,
or work crosses its outer boundary), so all of the entropy increase is internally generated:
$$s_{gen}=s_2-s_1=8.8242-7.7641=\boxed{1.060\ \text{kJ/kg}\cdot\text{K}}.$$
This is strictly positive, as required for the highly irreversible uncontrolled (unresisted)
expansion into a vacuum.