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22-Agric-A3 Heat Engineering · May 2013

Question 1 of 4: Steady Conduction Through a Lead Slab

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

Notes on this paper

Paper format. 04-Agric-A3 Heat Engineering, National Exams May 2013 — a three-hour open-book examination; any non-communicating calculator is permitted. The cover page states that four (4) questions constitute a complete exam paper and that only the first four as they appear in the answer book are marked, that each question is of equal value, and that all questions require calculation. All four printed problems are worked here.

Reference texts. Y.A. Çengel & A.J. Ghajar, Heat and Mass Transfer: Fundamentals and Applications, 5th ed. (conduction, flat-plate solar collectors); J.P. Holman, Heat Transfer, 10th ed. (natural-convection correlations and boundary-layer thickness); R.F. Barron, Cryogenic Heat Transfer, 2nd ed. (radiation shields for cryogenic lines).

Problem 1: Steady Conduction Through a Lead Slab (25 points)

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.

QuantityValue
Thermal conductivity of lead, k35 W/m·K
Front-face temperature, T₁110°C
Back-face temperature, T₂50°C
Slab area, A0.4 m²
Slab thickness, L0.03 m

Find. The heat flux q (W/m²) and the total heat transfer rate Q (W) through the slab.

Approach. One-dimensional steady conduction with no internal generation reduces to Fourier's law across the plane slab; the flux is uniform, so the rate is simply the flux times the face area.

A = 0.4 m², lead, k = 35 W/m·K q T₁ = 110°C T₂ = 50°C L = 0.03 m
One-dimensional conduction across the lead slab: heat flux q flows from the hot face (110°C) to the cold face (50°C) over the 0.03 m thickness.
  1. Heat flux from Fourier's law. For steady 1-D conduction across a plane wall, $$q = k\,\frac{T_1-T_2}{L} = 35\ \frac{\text{W}}{\text{m}\cdot\text{K}}\times \frac{110-50\ \text{K}}{0.03\ \text{m}} = \boxed{70{,}000\ \text{W/m}^2 = 70\ \text{kW/m}^2}$$
  2. Heat transfer rate. The flux is uniform over the face, so the rate is $$Q = q\,A = 70{,}000\ \frac{\text{W}}{\text{m}^2}\times 0.4\ \text{m}^2 = \boxed{28{,}000\ \text{W} = 28\ \text{kW}}$$
QuantityResult
Heat flux, q70,000 W/m² (70 kW/m²)
Heat transfer rate, Q28,000 W (28 kW)
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