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 small vertical plate dissipates a fixed heat load to still air by natural convection AND radiation acting together (in parallel, same $\Delta T$); both faces of the thin case are taken as active heat-transfer area.
| Quantity | Symbol | Value |
|---|---|---|
| Plate height (vertical, characteristic length) | $H$ | 40 mm |
| Plate width | $W$ | 50 mm |
| Ambient / surroundings temperature | $T_\infty$ | $25\,{}^{\circ}\text{C}$ |
| Surface emissivity | $\varepsilon$ | 0.82 |
| Heat dissipated | $\dot Q$ | 7 W |
Find. The steady surface temperature $T_s$.
Approach. Both faces of the case ($A=2HW$) lose heat by natural convection (Churchill–Chu correlation, valid for all Rayleigh numbers) and by radiation to the same $25\,{}^{\circ}\text{C}$ surroundings; because $h$ itself depends on $T_s$ through the film properties, solve $h(T_s)A(T_s-T_\infty)+\varepsilon\sigma A(T_s^4-T_\infty^4)=\dot Q$ iteratively.
| Quantity | Value |
|---|---|
| Rayleigh number $Ra_H$ | $3.03\times10^5$ |
| Convection coefficient $h$ | 9.08 W/m²·K |
| Surface temperature $T_s$ | $127.0\,{}^{\circ}\text{C}$ |
| Convective / radiative split | 3.70 W / 3.30 W |