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17-Phys-B6 Applied Thermodynamics and Heat Transfer · Undated paper

Question 7 of 8: Vertical Power-Amplifier Case — Combined Natural Convection and Radiation

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

Notes on this paper

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, sh​ell-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 7: Vertical Power-Amplifier Case — Combined Natural Convection and Radiation

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.

Given data
QuantitySymbolValue
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.

  1. Set up the coupled convection+radiation balance and iterate. With $A=2\times0.04\times0.05=0.004$ m² and air properties evaluated at the film temperature $T_f=(T_s+T_\infty)/2$ on each pass: $$Ra_H=\frac{g\beta(T_s-T_\infty)H^3}{\nu\alpha},\qquad Nu=\left\{0.825+\frac{0.387\,Ra_H^{1/6}}{\left[1+(0.492/Pr)^{9/16}\right]^{8/27}}\right\}^2,\qquad h=\frac{Nu\,k}{H}$$ $$h(T_s)A(T_s-T_\infty)+\varepsilon\sigma A(T_s^4-T_\infty^4)=\dot Q$$ converges (Newton iteration on $T_s$) to $$\boxed{T_s=127.0\,{}^{\circ}\text{C}\ (400.1\text{ K})}$$ with $Ra_H=3.03\times10^5$, $Nu=12.1$, $h=9.08$ W/m²·K.
  2. Split the 7 W between the two mechanisms as a check. $$q_{conv}=hA(T_s-T_\infty)=9.08\times0.004\times(127.0-25.0)$$ $$\boxed{q_{conv}=3.70\text{ W}}$$ $$q_{rad}=\varepsilon\sigma A(T_s^4-T_\infty^4)=0.82\times5.67\times10^{-8}\times0.004\times(400.1^4-298.15^4)$$ $$\boxed{q_{rad}=3.30\text{ W}}$$ $$q_{conv}+q_{rad}=3.70+3.30=7.00\text{ W}\ \checkmark$$
Question 7 — results
QuantityValue
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 split3.70 W / 3.30 W