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Chapter 4 Unsteady Conduction

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Chapter 4 delves into the intriguing world of unsteady conduction, a mode of heat transfer characterized by time-varying temperature distributions within a solid. This comprehensive chapter provides a detailed exploration of the underlying principles, mathematical models, and practical applications of unsteady heat conduction. The document covers the governing differential equation for unsteady heat conduction, also known as the heat diffusion equation. It introduces analytical and numerical methods used to solve transient heat conduction problems, enabling engineers and researchers to predict temperature variations over time. Various initial and boundary conditions are discussed, providing insights into their influence on the transient temperature response in different geometries and configurations. The chapter includes practical examples and case studies illustrating unsteady conduction phenomena in engineering applications. It explores the significance of transient heat transfer in fields such as electronics cooling, materials processing, and thermal management of energy systems. Furthermore, the document addresses practical aspects of time constants, Biot numbers, and Fourier numbers, crucial for understanding the time scales and transient behavior of heat conduction problems. Researchers, engineers, and students will find this chapter a valuable resource for comprehending the complexities of unsteady conduction and its implications in diverse industries and scientific domains. By gaining a deeper understanding of unsteady heat transfer, readers can optimize designs, predict thermal responses, and address time-dependent challenges across various engineering applications.

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Forsberg Heat Transfer
Chapter 4
Unsteady Conduction




Lumped Systems Analysis
For a "lumped system", all points in an object have the same
temperature at a given time. That is, T = T (t ).




The body is initially at Ti and is suddenly immersed in
a fluid at lower temperature T . There is then
convection from the body to the fluid.




1

, Rate of decrease in = Rate of heat flow from
internal energy of the body the body to the fluid
dT
−  cV = hA(T − T )
dt
V = volume of the body
A = surface area of the body
T = constant, so the above equation becomes
d (T − T ) hA
=− dt
T − T  cV
T −T
At t = 0, the body is at Ti d (T − T )
t
hA
At t = t , the body is at T 
Ti −T
T − T
=−
 cV 0
dt
Integrating, we get




 T − T  hA
ln   = − t
 Ti − T   cV
 hA 
− t
  cV 
T − T = (Ti − T ) e
 hA 
− t
  cV 
T (t ) = T + (Ti − T ) e
The instantaneous heat flow at any time t is
dT
q(t ) = −  cV = hA(T − T )
dt




2

, t
Q =  q(t ) dt is the amount of heat, Q, transferred
0

to the fluid over the period t = 0 to t = t.
We can use either
T
Q = −  cV  dT = −  cV [T (t ) − Ti ] or
Ti
t
Q = h A  [T (t ) − T ] dt
0

  hA 
− t 
The result is: Q =  cV (Ti − T ) 1 − e   cV  
 




Application Criterion for Lumped Analysis
The Biot number for lumped systems is
hL
Bilumped =
k
where:
h = convective coefficient at the surface
L = characteristic length for the body
= volume V / surface area A
k = thermal conductivity of the body
If Bilumped < 0.1 Lumped-System Analysis is applicable




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