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04-BS-10 · May 2016

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)

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. 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.

Find. (a) $T_2$ [°C]; (b) $V_A/V_{total}$ [%]; (c) $s_{gen}$ [kJ/kg·K].

Approach

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.

  1. Initial state. At 1.0 MPa, 500°C: $u_1=3124.99$ kJ/kg, $v_1=0.35411$ m$^3$/kg, $s_1=7.7641$ kJ/kg·K.
  2. 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: $$T_2=\boxed{495.69\ ^\circ\text{C}}\quad(v_2=3.5456\ \text{m}^3/\text{kg},\ s_2=8.8242\ \text{kJ/kg}\cdot\text{K}).$$
  3. 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: $$\frac{V_A}{V_{total}}=\frac{v_1}{v_2}=\frac{0.35411}{3.5456}=\boxed{0.0999\ (10.0\%)}.$$
  4. 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.
QuantityResult
(a) $T_2$495.69°C
(b) $V_A/V_{total}$9.99% (≈10%)
(c) $s_{gen}$1.060 kJ/kg·K
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