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)
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.
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.
Heat transfer rate (part a).
$$\dot Q=\dot m_{da}(h_2-h_1)=0.0762\times(33.78-23.65)=0.0762\times10.13
=\boxed{0.771\ \text{kW}}.$$