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04-BS-10 · May 2018

Question 8 of 9: Sensible Heating of Humid Air

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 8: Sensible Heating of Humid Air (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. Inlet: $P=95$ kPa, $T_1=15\ ^\circ$C, $\phi_1=30\%$, $\dot V_1=4$ m³/min. Exit: $T_2=25\ ^\circ$C. Sensible heating only (no moisture added or removed).

Find. (a) $\dot Q$ [kW]; (b) $\phi_2$.

Approach

A heating coil with no condensation or humidification keeps the humidity ratio $W$ (mass of water vapor per mass of dry air) constant across the section, so the exit state is fixed by $T_2$ and $W_2=W_1$. Convert the given volumetric flow rate to a dry-air mass flow rate using the inlet humid-air specific volume, then take the enthalpy difference at constant $W$ for the heat rate; the exit relative humidity follows directly once $T_2$ and $W_1$ are known.

  1. Inlet humid-air properties. At $P=95$ kPa, $T_1=15\ ^\circ$C, $\phi_1=0.30$: $$W_1=0.003382\ \text{kg water/kg dry air},\qquad h_1=23.65\ \text{kJ/kg dry air},\qquad v_1=0.8750\ \text{m}^3/\text{kg dry air}.$$
  2. Dry-air mass flow rate. $$\dot m_{da}=\frac{\dot V_1}{v_1}=\frac{4/60\ \text{m}^3/\text{s}}{0.8750} =\boxed{0.0762\ \text{kg dry air/s}}.$$
  3. Exit state at constant humidity ratio. With no moisture added, $W_2=W_1= 0.003382$. At $P=95$ kPa, $T_2=25\ ^\circ$C, $W_2=0.003382$: $$h_2=33.78\ \text{kJ/kg dry air},\qquad \phi_2=\boxed{0.1614\ (16.1\%)}.$$ The relative humidity drops even though no moisture is removed, because the saturation pressure of water rises sharply between 15°C and 25°C while the actual vapor pressure (set by $W_1$) stays fixed.
  4. Heat transfer rate (part a). $$\dot Q=\dot m_{da}(h_2-h_1)=0.0762\times(33.78-23.65)=0.0762\times10.13 =\boxed{0.771\ \text{kW}}.$$
QuantityResult
(a) $\dot Q$0.771 kW
(b) $\phi_2$0.1614 (16.1%)