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04-BS-10 · December 2015

Question 9 of 9: Rigid Tank Filled from a Supply Line, Isothermal

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 9: Rigid Tank Filled from a Supply Line, Isothermal (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. $V=0.5$ m$^3$, initially evacuated. Supply line: $P_{line}=100$ kPa, $T_{line}=21\ ^\circ$C. Final tank pressure $P_2=100$ kPa. Tank temperature held constant at $T=21\ ^\circ$C ($=294.15$ K) throughout by heat transfer.

Find. $Q$ [kJ].

Approach

This is an unsteady-flow (charging) problem, but with the unusual twist that heat transfer actively holds the tank temperature equal to the supply-line temperature throughout, so the final internal energy equals the line's internal energy exactly. Apply the uniform-flow energy balance with the mass balance ($m_{in}=m_2$, since the tank started evacuated) to solve directly for $Q$.

  1. Final mass in the tank. Ideal gas at $P_2=100$ kPa, $T=294.15$ K: $$m_2=\frac{P_2V}{RT}=\frac{100\times0.5}{0.287\times294.15}=\boxed{0.5923\ \text{kg}}.$$
  2. Energy balance. Uniform-flow first law for the tank (no initial mass, no work, mass entering carries the line's flow enthalpy $h_{line}$): $$Q=m_2u_2-m_{in}h_{line}=m_2u_2-m_2h_{line}=m_2(u_2-h_{line}).$$ Since the tank temperature is held at $T_{line}$ throughout, $u_2=u_{line}$ (ideal gas, $u=u(T)$ only), so: $$u_2-h_{line}=u_{line}-h_{line}=-RT_{line}.$$
  3. Heat transfer. $$Q=-m_2RT_{line}=-0.5923\times0.287\times294.15\ \text{kJ}.$$ Recognizing $m_2RT_{line}=P_2V$ exactly (the same ideal-gas law used to find $m_2$), this collapses to the closed form: $$Q=-P_2V=-100\times0.5=\boxed{-50.00\ \text{kJ}}.$$ The negative sign shows heat must be REJECTED from the tank to hold its temperature constant while being charged — the flow work carried in by the entering air would otherwise raise the tank's temperature above the line's.
QuantityResult
$m_2$0.5923 kg
$Q$−50.00 kJ
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