17-Phys-B6 Applied Thermodynamics and Heat Transfer · May 2013
Question 5 of 8: Critical Radius of Pipe Insulation
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. 98-Phys-B6 Applied Thermodynamics and Heat Transfer,
National Examination May 2013 — an open-book examination (any textbook, reference or
non-communicating calculator permitted). Part A (Thermodynamics, Q1–4) and Part B (Heat
Transfer, Q5–8) together form the paper; a complete exam is five answers, drawn either
three-from-A/two-from-B or two-from-A/three-from-B. Every question is nonetheless answered in
full below so the paper remains a complete study resource. All eight questions carry equal
value in the grading.
Reference texts. Y. A. Çengel & M. A. Boles, Thermodynamics: An
Engineering Approach, 8th ed. (ideal-gas cycles, vapour power cycles with reheat, gas
compressors, vapour-compression refrigeration); F. P. Incropera & D. P. DeWitt,
Fundamentals of Heat and Mass Transfer, 7th ed. (critical radius of insulation,
internal/external forced convection correlations, natural convection from horizontal cylinders,
radiation exchange, LMTD/effectiveness–NTU heat-exchanger analysis).
Given. Bare pipe diameter $d_i=1.27$ cm ($r_i=0.635$ cm), pipe
surface uniformly at $T_i=82.5^{\circ}\text{C}$; insulation $k=0.156$ W/m·K; ambient
$T_\infty=20^{\circ}\text{C}$, outer-surface $h=8.5$ W/m²·K.
Find. The insulation thickness(es) for which heat loss EXCEEDS the bare-pipe
loss.
Approach. This is a small-diameter pipe, so it is worth checking the
critical radius of insulation $r_{cr}=k/h$ before assuming insulation helps at all; heat loss per
unit length as a function of outer radius $r_o$ is then solved against the bare-pipe baseline.
Bare-pipe heat loss (baseline).
$$q'_{bare}=2\pi r_i h(T_i-T_\infty)=2\pi(0.00635)(8.5)(62.5)=\boxed{21.20\ \text{W/m}}.$$
Critical radius of insulation.
$$r_{cr}=\frac{k}{h}=\frac{0.156}{8.5}=\boxed{1.835\ \text{cm}},$$
which is nearly THREE TIMES the bare pipe's own radius ($r_i=0.635$ cm). Because
$r_{cr}>r_i$, adding insulation initially INCREASES total heat loss (the added convective
surface area outpaces the added conduction resistance) — the classic small-pipe critical-radius
effect. Heat loss per unit length as a function of outer radius, wall conduction neglected per
the problem statement, is
$$q'(r_o)=\frac{T_i-T_\infty}{\dfrac{\ln(r_o/r_i)}{2\pi k}+\dfrac{1}{2\pi r_o h}}.$$
At $r_o=r_{cr}$, $q'=29.72$ W/m — a $40\%$ INCREASE over the bare pipe, the worst case.
Crossover radius (root-find $q'(r_o)=q'_{bare}$, $r_o\neq r_i$). $q'(r_o)$
rises from $q'_{bare}$ at $r_o=r_i$, peaks at $r_{cr}$, then falls back through $q'_{bare}$ again
at a larger radius. Solving numerically (bisection) for that second crossing,
$$r^{*}=\boxed{9.40\ \text{cm}}\quad\Rightarrow\quad t^{*}=r^{*}-r_i=9.40-0.635=\boxed{8.77\ \text{cm}}.$$
Answer. ANY insulation thickness in the open interval
$$0 \lt t \lt 8.77\ \text{cm}$$
gives MORE heat loss than the bare pipe (worst at $t=r_{cr}-r_i=1.20$ cm, $+40\%$). Only
past $t\approx8.77$ cm does adding more insulation finally reduce the loss below the
bare-pipe value — a substantial, impractically thick jacket for a 1.27 cm pipe, which
is itself the point of the problem: on pipes this small, "a little insulation" is
counter-productive.