22-Mec-A1 Applied Thermodynamics and Heat Transfer · December 2016
Question 5 of 8: Heat Loss from a Pipe Before and After Adding Insulation
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Reference texts: Çengel & Boles, Thermodynamics: An Engineering Approach (9th ed., McGraw-Hill) — closed- and open-system energy balances, boundary work, reciprocating-compressor and vapour/gas power cycles, and gas-turbine refrigeration; Çengel & Ghajar, Heat and Mass Transfer (6th ed.) and Incropera, DeWitt, Bergman & Lavine, Fundamentals of Heat and Mass Transfer (8th ed., Wiley) — radial composite-wall conduction, internal-flow decay, natural convection with radiation from a horizontal cylinder, and the ε–NTU cross-flow heat-exchanger method. Air and steam properties are evaluated from IAPWS-IF97 / ideal-air data; the gas-turbine cycle uses cold-air-standard constant specific heats.
Paper format: National Examination 07-Mec-A1, December 2016, 3 hours, open book. Part A — Thermodynamics (Q1–4); Part B — Heat Transfer (Q5–8). Each answer carries equal value; a complete paper is any five (three from one part and two from the other). All eight questions are solved in full below.
Question 5: Heat Loss from a Pipe Before and After Adding Insulation (equal value)
Figure 5 — Radial layers pipe→A→B→C. The known conductivity of C fixes its resistance and hence the "after" heat rate; that pins the combined A+B resistance, which (being unchanged) then gives the "before" heat rate from the original 360 °C drop.
Approach. Insulation C is the only layer with a known conductivity, so its measured 150 °C drop gives the "after" heat rate; steady-state continuity then fixes the combined A+B resistance, which is a fixed property of the (unchanged) inner layers and delivers the "before" heat rate.
Resistance of layer C. $R'_C=\dfrac{\ln(r_3/r_2)}{2\pi k_C}=\dfrac{\ln(0.235/0.215)}{2\pi(0.2)}=0.0708$ m·°C/W.
Heat rate after adding C. The 180→30 °C drop is entirely across C:
$$q'_\text{after}=\frac{180-30}{R'_C}=\frac{150}{0.0708}$$
==**$q'_\text{after}\approx2119$ W/m.**==
Combined A+B resistance. In the "after" state the same $q'$ crosses A and B under a 500→180 °C drop:
$$R'_{A+B}=\frac{500-180}{q'_\text{after}}=\frac{320}{2119}=0.1510\ \text{m}\cdot\text{°C/W}$$
Heat rate before adding C. A and B are physically unchanged, so with the original 400→40 °C drop,
$$q'_\text{before}=\frac{400-40}{R'_{A+B}}=\frac{360}{0.1510}$$
==**$q'_\text{before}\approx2384$ W/m.**==
Check
The method needs no individual $k_A$, $k_B$: the two operating states share the same fixed $R'_{A+B}$, so one measured state calibrates it for the other. Adding C lowers the loss (2384 → 2119 W/m) even though the pipe now runs hotter (500 vs 400 °C) — the extra resistance more than offsets the larger driving temperature. The conductivities are assumed temperature-independent between the two states.