Case 1
Given,
d = 1m (Diameter of spherical tank)
t1 = 120℃ = 393K (Temperature of sphere)
t2 = 15℃ = 288K (Temperature of surrounding environment)
h = 25 W/m2K (Convective heat transfer coefficient of surrounding environment)
Find: (1) Q (Heat transfer rate)
Solution:
Heat transfer rate
Q1 = dtR = t1 - t21h. As = 393 - 288125 × 4π × 0.52
Q1 = 8246.68 W
Case 2
Given,
d = 1m (Diameter of spherical tank)
t1 = 120℃ = 393K (Temperature of sphere)
t3 = 15℃ = 288K (Temperature of surrounding environment)
h = 25 W/m2K (Convective heat transfer coefficient of surrounding environment)
K = 20 × 10 - 3W/mK (Thermal conductivity of urethane)
t2 = 40℃ = 313K (Outer temperature of urethane)
Find:
(1) T (Thickness of urethane)
(2) % Reduction in Q (After applying the insulation)
Solution:
Heat transfer rate
Q2 = dtR1 = t1 - t2r2 - r14π.K.r2r1 = 393 - 313r2 - 0.54π × 20 × 10 - 3 × r2 × 0.5
Q2 = 80(r2 - 0.5)0.125r2 …(1)
also,
Q2 = dtR2 = t2 - t31h. As = t2 - t31h × 4π × r22 = 313 - 288125 × 4π × r22
Q2 = 251100π × r22 …(2)
Equating (1) and (2)
80(r2 - 0.5)0.125r2 = 251100π × r22
80100π × r22 = 25(r2 - 0.5)0.125r2
10 = 7853.981r22 - 3926.99r2
r2 = 0.502m
Thickness of urethane
T = r2 - r1 = 0.502 - 0.5
T = 0.002m = 2mm
∴Q2 = 251100π × 0.5022
Q2 = 1979.234 W
% Reduction in Q
%↓Q = Q1 - Q2Q1 × 100 = 8246.68 - 1979.2348246.68 × 100
%↓Q = 75.99 %