Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams December 2013 — 04-Agric-A3, Heat Engineering (3 hours, open book). Four questions constitute a complete exam paper; each is of equal value (25 points) and all require calculation.
Reference texts: Çengel & Ghajar, Heat and Mass Transfer: Fundamentals and Applications (conduction, solar-collector performance testing); J.P. Holman, Heat Transfer (natural-convection correlations, boundary-layer thickness); R.F. Barron, Cryogenic Heat Transfer (concentric-cylinder radiation shields).
Approach. One-dimensional steady conduction with no internal generation reduces to Fourier's law across the plane slab; with Q, k, A and L already known, invert the law to solve directly for the unknown back-face temperature.
One-dimensional conduction across the slab: a steady 3 kW flows from the known hot face (415°C) through the 2.5 cm thickness to the unknown back face.
Invert Fourier's law for the unknown back-face temperature. For steady 1-D conduction across a plane wall, $Q = kA(T_1-T_2)/L$, so
$$T_2 = T_1 - \frac{Q\,L}{kA} = 415 - \frac{3000\ \text{W}\times0.025\ \text{m}}{0.2\ \dfrac{\text{W}}{\text{m}\cdot\text{K}}\times10\ \text{m}^2}
= 415 - 37.5 = \boxed{377.5\,{}^{\circ}\text{C}}$$
The 37.5°C drop across just 2.5 cm reflects the slab's low thermal conductivity (0.2 W/m·K is typical of a firebrick or low-density refractory, not a metal), which is why even a modest 3 kW load through a fairly large 10 m² face produces a temperature difference this size.
This slab problem is a direct inversion of the same steady-state conduction law used throughout the rest of this paper's collector and radiation problems: whichever of Q, T₁, T₂, k, A or L is unknown, the other five pin it down uniquely because the temperature profile through a plane wall with no internal generation is always linear.