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04-BS-10 · May 2018

Question 9 of 9: H₂/N₂ Mixture, Constant-Pressure Heating

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

Notes on this paper

National Exam 04-BS-10, Thermodynamics — May 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). 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, H₂, humid air) were computed from high-accuracy equations of state in place of printed property-table interpolation; every boxed numeric result.

Question 9: H₂/N₂ Mixture, Constant-Pressure Heating (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. $m_{H_2}=6$ kg, $m_{N_2}=21$ kg, $T_1=160$ K, $T_2=200$ K, constant pressure ($P=5$ MPa, does not enter the ideal-gas enthalpy calculation). Ideal-gas mixture.

Find. $Q$ [kJ].

Approach

A piston-cylinder at constant pressure with no other work mode gives $Q=\Delta H$ for the whole mixture. Because each component of an ideal-gas mixture behaves as if it alone occupied the volume at the mixture temperature, the total enthalpy change is simply the mass-weighted sum of each pure component's enthalpy change between $T_1$ and $T_2$ — evaluated here from each gas's own ideal-gas enthalpy function (temperature-only dependence, so the actual 5 MPa is irrelevant to the ideal-gas result).

  1. Per-component ideal-gas enthalpy change, H₂. From 160 K to 200 K: $$h_{H_2}(200)-h_{H_2}(160)=2557.13-2028.67=528.46\ \text{kJ/kg}.$$ $$Q_{H_2}=m_{H_2}\times528.46=6\times528.46=\boxed{3170.8\ \text{kJ}}.$$
  2. Per-component ideal-gas enthalpy change, N₂. From 160 K to 200 K: $$h_{N_2}(200)-h_{N_2}(160)=207.00-165.20=41.80\ \text{kJ/kg}.$$ $$Q_{N_2}=m_{N_2}\times41.80=21\times41.80=\boxed{877.8\ \text{kJ}}.$$
  3. Total heat transfer. Constant-pressure, piston-cylinder (boundary work only): $$Q=\Delta H=Q_{H_2}+Q_{N_2}=3170.8+877.8=\boxed{4048.6\ \text{kJ}}.$$ H₂'s small mass fraction (6 of 27 kg, 22%) nonetheless supplies about 78% of the total heat transfer, because hydrogen's per-kilogram specific heat is roughly 14× nitrogen's (its molar mass is about 14× smaller for a similar molar $c_p$).
QuantityResult
$Q$4048.6 kJ
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