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04-BS-10 · December 2018

Question 8 of 9: Air Turbine — Power and Exit Area

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

National Exam 04-BS-10, Thermodynamics — December 2018. 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 — the closest tabular value may be used). 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, O₂, humid air) were computed from high-accuracy equations of state in place of printed property-table interpolation; every boxed numeric result.

Question 8: Air Turbine — Power and Exit Area (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. $\dot m=10$ kg/s. Inlet: $P_1=500$ kPa, $T_1=900$ K, $V_1\approx0$. Exit: $P_2=100$ kPa, $T_2=600$ K, $V_2=100$ m/s. Adiabatic, steady, negligible PE.

Find. (a) $\dot W$ [kW]; (b) $A_2$ [m²].

Approach

Apply the steady-flow energy equation with the exit kinetic-energy term retained (the inlet term is explicitly negligible) using real variable-specific-heat air enthalpies, then size the exit area from the ideal-gas continuity equation at the exit state.

  1. Power developed (part a). Steady-flow energy balance, $\dot Q\approx0$, $\Delta pe\approx0$: $$\dot W=\dot m\left[(h_1-h_2)-\frac{V_2^2-V_1^2}{2}\right] =\dot m\left[(h_1-h_2)-\frac{V_2^2}{2}\right]$$ using real air enthalpies $h(900\ \text{K})=1059.40$, $h(600\ \text{K})=733.42$ kJ/kg: $$\dot W=10\left[(1059.40-733.42)-\frac{100^2}{2\times1000}\right]=10\,[325.99-5.00]=10\times320.99$$ $$=\boxed{3209.9\ \text{kW}}.$$
  2. Exit specific volume and area (part b). Ideal gas at the exit state: $$v_2=\frac{RT_2}{P_2}=\frac{0.287\times600}{100}=1.7220\ \text{m}^3/\text{kg}.$$ Continuity, $\dot m=\rho_2 A_2V_2=A_2V_2/v_2$: $$A_2=\frac{\dot m\,v_2}{V_2}=\frac{10\times1.7220}{100}=\boxed{0.1722\ \text{m}^2}.$$
QuantityResult
(a) $\dot W$3209.9 kW
(b) $A_2$0.1722 m²