25-Nav-A1 Fundamentals of Naval Architecture · May-98-Mar-A1 2016
Question 5 of 8: Insulating a Steam Tube to Cut Heat Loss by 95%
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Examinations, May 2016 — 98-Mar-A1 Applied Thermodynamics and Heat Transfer, 3 hours, open book (Part A: Thermodynamics, Part B: Heat Transfer; 5 of 8 questions required, all 8 answered below for full study coverage).
Reference texts: Cengel & Boles, Thermodynamics: An Engineering Approach; Sonntag, Borgnakke & Van Wylen, Fundamentals of Thermodynamics; Incropera & DeWitt, Fundamentals of Heat and Mass Transfer.
It is solved as the thermodynamics/heat-transfer exam it actually is.
Question 5: Insulating a Steam Tube to Cut Heat Loss by 95%
Given. A bare copper tube loses heat to the surroundings by forced convection; insulation is added on the outside to cut that loss by 95%.
Given data
Quantity
Symbol
Value
Tube outside diameter
$D$
2.54 cm
Inside surface temperature
$T_i$
100°C
Room (air) temperature
$T_\infty$
27°C
Insulation conductivity
$k$
0.0875 W/m·K
Convection coefficient
$h$
55 W/m²·K
Find. Insulation thickness $t$ for a 95% reduction in heat loss per unit length, and the resulting outer-surface temperature $T_o$. (Copper's thermal conductivity is very high, so the tube-wall resistance is negligible — the insulation's inner surface is effectively at $T_i=100^\circ\text{C}$.)
Bare-tube heat loss per unit length. With the outer copper surface directly exposed to convection, $r_1=D/2=0.0127\text{ m}$:
$$q'_{bare}=h\pi D(T_i-T_\infty)=55\pi(0.0254)(73)$$
$$\boxed{q'_{bare}\approx320.4\text{ W/m}}$$
Target heat loss with insulation. A 95% cut means only 5% remains: $q'_{target}=0.05(320.4)=16.02\text{ W/m}$.
Series conduction + convection resistance. With insulation to outer radius $r_2$:
$$q'=\frac{T_i-T_\infty}{\dfrac{\ln(r_2/r_1)}{2\pi k}+\dfrac{1}{h\,2\pi r_2}}$$
Solving numerically for $r_2$ (the equation is implicit since $r_2$ appears in both the log term and the convection term) gives $r_2\approx0.1540\text{ m}$, so
$$\boxed{t=r_2-r_1\approx0.1540-0.0127\approx0.1413\text{ m}\ (\approx14.1\text{ cm})}$$
Outer surface temperature. From the convection leg alone, $q'=h\,2\pi r_2(T_o-T_\infty)$:
$$T_o=T_\infty+\frac{q'}{h\,2\pi r_2}=27+\frac{16.02}{55(2\pi)(0.1540)}$$
$$\boxed{T_o\approx27.3^\circ\text{C}}$$