Thermodynamics- Multidimensional and Transient Conduction Flashcards
What heat equation can be taken for a fluid running through a cylinder under steady state, no heat generation and axisymmetry?
d/dr(krdT/dr)=0
Thermal resistance formula for conduction out of a tube radially
R=ln(r2/r1)/2πLk
Where L is length of pipe interested in
r is radius from centre of flowing fluid to boundary
Formula for temperature distribution in the walls of a pipe
T(r)=((Ts1-Ts2)/ln(r1/r2))ln(r/r2)+Ts2
Where Ts1 is temperature of inner face of tube
Ts2 is temperature of outer face of tube
r1 and r2 follow same principle
Solution methods to 2D conduction
Exact: like separation of variables
Graphical: like trapezium rule
Numerical: finite-difference/element or boundary-element method
How does finite-difference method work?
It seems pointless.
Represent the physical system by a nodal network, grid or mesh. In 1D we solve along a line and break it up into points. Basically change in y over change in x for two points equidistant from the point you want. This is second order so the points are already derivatives.
Approximate formula for finite-differences method
d/dx(kdT/dx)=k(T1-2T0+T-1)/Δx^2=0
Transient conduction
A heat transfer process for which the temperature varies with time as well as location within a solid
dT/dt=kdT/dx
Where all ds are curly
What does the lumped capacitance method assume about dT/dx (curly)?
It equals 0 so there is a spatially uniform temperature distribution
What does the rate of change in energy stored equal in the lumped capacitance method?
ρVcdT/dt
Basically mCpdT/dt
This is all equal to energy in minus out plus generated which can come from radiation and convection
Formula for Biot number
Bi=hLc/k
h is convective or radiative heat transfer coefficient
k is thermal conductivity
Lc is characteristic length of solid (V/As)
What is the criterion for the applicability of the lumped capacitance method?
Bi«1
Means k is high so dT/dx is about 0 from:
dT/dx=-q/k
With lumped capacitance method, what equation can be formed if negligible radiation and heat generation?
ρVcdT/dt=-hA(T-Tinf)
Formula for thermal time constant
τt=(1/hA)ρVc
t is subscript
Basically thermal resistance times thermal capacitance
Formula for change in thermal energy stored
ΔEst=-(ρVc)θ(1-e^(-t/τ))
θ is T-Tinf