Interface conditions for heat transfer

AI Thread Summary
The discussion focuses on interface conditions for heat transfer between materials and fluids. In perfect contact scenarios, the temperature and heat flux continuity conditions are established, with specific equations for thermal conductivity and diffusivity. When a fluid flows over a solid, the heat transfer is modeled using a film coefficient, which relates the heat flux to the temperature difference between the fluid and the solid surface. The conversation also touches on the application of Newton's law of cooling in this context. The need for clarity regarding the conditions of the solid's surrounding fluid domain is emphasized.
jens000
Messages
2
Reaction score
0
I have two different scenarios for heat transfer I need some help with understanding.

1.) Given two different materials in perfect contact with each other with no thermal resistance at the interface, what are the interface conditions at the interface? Considering two heat equations with variables T1 and T2, the possible conditions would be
I.) T1 = T2 and \kappa_1 T1_x = \kappa_2 T2_x,
II.) T1 = T2 and \alpha_1 T1_x = \alpha_2 T2_x
where \kappa_{1,2} is the thermal conductivity and \alpha_{1,2} is the thermal diffusivity. From a mathematical point of view, both give a well-posed coupling but only one should represent real physics.

2.) Same situation, but with a fluid flowing over a solid?
 
Science news on Phys.org
For two solids, continuity exists both in temperature and heat flux. In one dimension,
k1dt/dn = k2dt/dn at n=interface. The temperature condition you have already noted.

For fluid flowing over a solid, the situation is linked by using a film coefficient such that the heat flux at the solid equals a film coefficient multiplied by the difference in bulk fluid temperature and the surface temperature of the object. It is generally considered a boundary condition (commonly called the mixed condition). That is how it is mathematically handled.

There are formulas that provide the film coefficient based on whether the flow is laminar or turbulent based on fluid properties such as density, viscosity, specific heat, and fluid conductivity. Velocity is also important.
 
If, per chance, you are trying to solve the Fourier equation for transient heat transfer in one dimension by separation of variables and your domain in space consists of two different solids with differing thermal properties, you have to use what is called discontinuous weighting functions to maintain orthogonality of eigenfunctions.
 
Thank you for the reply! It was along the lines I had expected. Is it Newton's law of cooling you refer to in the fluid/solid problem? I was considering a situation when the solid is not surrounded by a fluid domain big enough such that the heat transfer can be modeled by a boundary condition.
 
jens000 said:
Thank you for the reply! It was along the lines I had expected. Is it Newton's law of cooling you refer to in the fluid/solid problem? I was considering a situation when the solid is not surrounded by a fluid domain big enough such that the heat transfer can be modeled by a boundary condition.

Yes, the mixed bc is Newton's law of cooling.

"I was considering a situation when the solid is not surrounded by a fluid domain big enough such that the heat transfer can be modeled by a boundary condition."

Can you be more specific? I'm not sure what you are alluding to here.
 
I was watching a Khan Academy video on entropy called: Reconciling thermodynamic and state definitions of entropy. So in the video it says: Let's say I have a container. And in that container, I have gas particles and they're bouncing around like gas particles tend to do, creating some pressure on the container of a certain volume. And let's say I have n particles. Now, each of these particles could be in x different states. Now, if each of them can be in x different states, how many total...
Thread 'Why work is PdV and not (P+dP)dV in an isothermal process?'
Let's say we have a cylinder of volume V1 with a frictionless movable piston and some gas trapped inside with pressure P1 and temperature T1. On top of the piston lay some small pebbles that add weight and essentially create the pressure P1. Also the system is inside a reservoir of water that keeps its temperature constant at T1. The system is in equilibrium at V1, P1, T1. Now let's say i put another very small pebble on top of the piston (0,00001kg) and after some seconds the system...
Back
Top