22-Mec-A1 Applied Thermodynamics and Heat Transfer · May 2015
Question 5 of 8: Self-Cleaning Oven Composite Window
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper: National Examinations — 07-Mec-A1 Applied Thermodynamics and Heat Transfer, May 2015. Open-book, 3-hour paper. Part A (Thermodynamics, Q1–Q4) and Part B (Heat Transfer, Q5–Q8); a complete paper is any five questions — three from one part and two from the other, all of equal value. Full worked solutions to all eight questions are given below.
Reference texts: Çengel & Boles, Thermodynamics: An Engineering Approach (9th ed., McGraw-Hill) — closed- and open-system energy balances, steam tables, vapour and gas power cycles and vapour-compression refrigeration; Çengel & Ghajar, Heat and Mass Transfer (6th ed.) and Incropera, DeWitt, Bergman & Lavine, Fundamentals of Heat and Mass Transfer (8th ed., Wiley) — composite-wall conduction, internal-flow and cross-flow convection correlations, natural convection with radiation, and the ε–NTU / LMTD-correction heat-exchanger methods. Freon-12 property data are taken from the appendix supplied with the exam; steam, air and water data from standard tables.
Given. Series composite window with $L_A=3L_B$, $k_A=0.18$, $k_B=0.10\ \text{W/m}\cdot\text{K}$. Inside the oven, convection and radiation act in parallel ($h_i=h_r=25$, both from 500 °C); outside, convection $h_o=25\ \text{W/m}^2\text{K}$ to the 25 °C room. Safety limit $T_o\le50\ ^\circ\text{C}$.
Find. The minimum total plastic thickness $L_A+L_B$.
Figure 4 — Equivalent thermal network per unit area: the inside convective and radiative resistances act in parallel (combined $1/(h_i+h_r)=1/50$), in series with the two plastic conduction resistances and the outside convective film $1/h_o$.
Approach. The outside surface temperature is fixed by the heat that must be convected away at that surface; setting $T_o=50\ ^\circ\text{C}$ gives the maximum allowable flux, which in turn fixes the minimum total series resistance and hence the plastic thickness.
Maximum allowable flux. At the outer surface all the through-flux leaves by convection, so at the 50 °C limit$$q''=h_o(T_o-T_\infty)=25(50-25)=\boxed{625\ \text{W/m}^2}.$$
Required total resistance. The same flux is driven by the full 500 → 25 °C difference through the series network:$$R''_\text{tot}=\frac{T_a-T_\infty}{q''}=\frac{500-25}{625}=0.760\ \tfrac{\text{m}^2\text{K}}{\text{W}}.$$
Isolate the plastic resistance. Subtract the inside (parallel) and outside film resistances:$$\frac{L_A}{k_A}+\frac{L_B}{k_B}=R''_\text{tot}-\frac{1}{h_i+h_r}-\frac{1}{h_o}=0.760-0.020-0.040=0.700\ \tfrac{\text{m}^2\text{K}}{\text{W}}.$$
Apply $L_A=3L_B$ and solve. $$\frac{3L_B}{0.18}+\frac{L_B}{0.10}=16.667L_B+10L_B=26.667L_B=0.700\;\Rightarrow\;L_B=0.0263\ \text{m},$$ so $L_A=0.0788$ m and$$L_A+L_B=\boxed{0.105\ \text{m}=10.5\ \text{cm}}.$$
Check
A thicker window raises the series resistance, lowers the through-flux, and therefore lowers $T_o$; the 10.5 cm value is the minimum that just holds $T_o=50\ ^\circ\text{C}$. Placing the inside convective and radiative coefficients in parallel (both driven from the same 500 °C source to the same inner surface) is essential — treating them in series would badly overstate the inside resistance.