17-Phys-B6 Applied Thermodynamics and Heat Transfer · Undated paper
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Paper format. 17-Phys-B6 Applied Thermodynamics and Heat Transfer, National Examinations, May 2019 — a three-hour open-book examination; candidates are expected to bring both a thermodynamics text and a heat-transfer text to make use of the property tables and graphs the exam supplies. A complete examination is five questions — either three from Part A (Thermodynamics, Q1–Q4) and two from Part B (Heat Transfer, Q5–Q8), or two from Part A and three from Part B — every question carrying equal value; all eight are solved below as a complete study set.
Reference texts. Y. A. Çengel and M. A. Boles, Thermodynamics: An Engineering Approach, 8th ed. (polytropic closed-system processes, throttling, Rankine-cycle reheat/extraction turbines, air-standard Brayton-cycle energy balances, vapour-compression refrigeration); F. P. Incropera and D. P. DeWitt, Fundamentals of Heat and Mass Transfer, 7th ed. (composite plane-wall conduction with convection and radiation at both faces, combined entry-length internal convection, natural convection with radiation from a vertical plate, shell-and-tube heat exchanger sizing via the LMTD correction-factor method). Ammonia, steam and R-134a property values were computed (Bell et al., IAPWS-95 / REFPROP-quality equations of state) and cross-checked against the printed saturated-ammonia appendix table on page 6 of the source exam, which it matched to 3–4 significant figures.
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. A two-layer plastic window separates the $500\,{}^{\circ}\text{C}$ oven interior from $25\,{}^{\circ}\text{C}$ room air; convection AND radiation act in PARALLEL on the hot (inside) face (same driving $\Delta T$, so their coefficients simply add), while only convection acts on the cool (outside) face.
| Quantity | Symbol | Value |
|---|---|---|
| Oven air / wall temperature | $T_a=T_w$ | $500\,{}^{\circ}\text{C}$ |
| Room air temperature | $T_o$ | $25\,{}^{\circ}\text{C}$ |
| Max. outside surface temperature | $T_{s,o}$ | $50\,{}^{\circ}\text{C}$ |
| Inside convection coefficient | $h_{ci}$ | 25 W/m²·K |
| Inside radiation coefficient | $h_r$ | 25 W/m²·K |
| Outside convection coefficient | $h_\infty$ | 25 W/m²·K |
| Thermal conductivity, layer A | $k_A$ | 0.18 W/m·K |
| Thermal conductivity, layer B | $k_B$ | 0.10 W/m·K |
| Thickness relation | $L_A$ | $3L_B$ |
Find. The minimum total window thickness $L_A+L_B$ that keeps $T_{s,o}\le50\,{}^{\circ}\text{C}$.
Approach. At the LIMITING design point $T_{s,o}=50\,{}^{\circ}\text{C}$ exactly, the outside convection alone fixes the heat flux; the same flux must cross the inside-convection resistance and both conduction resistances in series between the oven and that outside surface, which is one equation in the one unknown $L_B$ (via $L_A=3L_B$).
| Quantity | Value |
|---|---|
| Thickness of B, $L_B$ | 26.25 mm |
| Thickness of A, $L_A$ | 78.75 mm |
| Minimum total thickness $L_A+L_B$ | 105.0 mm |