Combining two thermal conductivity (k) values

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SUMMARY

The discussion focuses on the application of thermal conductivity values in heat transfer scenarios involving two materials with different thermal conductivities. The formula Q/t = A(T2-T1)/ L1/k1 + L2/k2 is utilized for steady-state heat flow, while Newton's Law of Cooling, represented as dT/dt = -k (T initial - T surroundings), is applied for cooling processes. A specific example is provided with Neon gas (k = 0.0116 cal/sec) transferring heat through a copper container (k = 0.92 cal/sec), highlighting the complexities introduced by convective heat transfer and the need for the convective heat transfer coefficient.

PREREQUISITES
  • Understanding of thermal conductivity and its measurement
  • Familiarity with Newton's Law of Cooling
  • Knowledge of heat transfer principles, including conduction and convection
  • Ability to calculate convective heat transfer coefficients
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  • Research the derivation and applications of the formula Q/t = A(T2-T1)/ L1/k1 + L2/k2
  • Learn about the calculation of convective heat transfer coefficients in gases
  • Study transient conduction heat transfer problems and their solutions
  • Explore the effects of boundary layer thickness on heat transfer rates
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Engineers, physicists, and students in thermal dynamics or heat transfer, particularly those dealing with multi-material systems and transient heat conduction problems.

morrobay
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In the case when heat is flowing at a steady state through two materials with different
thermal conductivities, the classic Q/t = A(T2-T1)/ L1/k1 + L2/k2 applies. In this case T2 is fixed and the two different k values are combined.
In the case of cooling , Newtons Law of Cooling applies dT/dt = -k ( T initial - T surroundings)
With solution T(t)= T surr +(T ini - T surr)e^-kt
Regarding Newtons Law of Cooling:
If the heat is being transferred through a container wall with a different (k) than the material
that is cooling how can two thermal conductivites be applied in the solution to Newtons Law of cooling ?
For example suppose a gas ,Neon, with a thermal conductivity (k) of .0116 cal/sec
is transferring heat through a copper walled container, Cu (k) = .92 cal /sec.
 
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This is not a straightforward problem. There is convective heat transfer in the Neon which may provide a resistance. One needs to know the convective heat transfer coefficient between the wall and the neon, or, equivalently, the convective boundary layer thickness. As a worst case, one could assume that there is no convection, and the neon could be treated as a rigid body, in which case one would be faced with a transient conduction heat transfer problem, including heat conduction throughout the neon.
 

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