Appendices 10.A & 10.B: An Educational Presentation
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Transcript of Appendices 10.A & 10.B: An Educational Presentation
Appendices 10.A & 10.B:An Educational
PresentationPresented By:
Joseph AshJordan Baldwin
Justin HirtAndrea Lance
History of Heat Conduction
Jean Baptiste Biot (1774-1862)
French Physicist Worked on analysis of
heat conduction Unsuccessful at dealing
with the problem of incorporating external convection effects in heat conduction analysis
History of Heat Conduction
Jean Baptiste Joseph Fourier (1768 – 1830) Read Biot’s work 1807 determined how to solve the
problem Fourier’s Law
Time rate of heat flow (Q) through a slab is proportional to the gradient oftemperature difference
History of Heat Conduction
Ernst Schmidt German scientist Pioneer in Engineering
Thermodynamics Published paper “Graphical Difference
Method for Unsteady Heat Conduction” First to measure velocity and
temperature field in free convection boundary layer and large heat transfer coefficients
Schmidt Number Analogy between heat and mass transfer that causes a dimensionlessquantity
Derivation of the Heat Conduction
EquationA first approximation of the equations that govern the conduction of heat in a solid rod.
Consider the following:
A uniform rod is insulated on both lateral ends. Heat can now only flow in the axial direction.
It is proven that heat per unit time will pass from the warmer section to the cooler one.
The amount of heat is proportional to the area, A, and to the temperature difference T2-T1, and is inversely proportional to the separation distance, d.
The final consideration can be expressed as the following:
is a proportionality factor called the thermal conductivity and is determined by material properties
Assumptions
The bar has a length L so x=0 and x=L Perfectly insulated Temperature, u, depends only on position, x,
and time, t Usually valid when the lateral dimensions are
small compared to the total length.
The differential equation governing the temperature of the bar is a physical balance between two rates:
Flux/Flow term Absorption term
Flux
The instantaneous rate of heat transfer from left to right across the cross sections x=x0 where x0 is arbitrary can be defined as:
The negative is needed in order to show a positive rate from left to right (hot to cold)
Flux
Similarly, the instantaneous rate of heat transfer from right to left across the cross section x=x0+Δx where Δx is small can be defined as:
Flux
The amount of heat entering the bar in a time span of Δt is found by subtracting the previous two equations and then multiplying the result by Δt:
Heat Absorption
The average change in temperature, Δu, can be written in terms of the heat introduced, Q Δt and the mass Δm of the element as:
where s = specific heat of the materialρ = density
Heat Absorption
The actual temperature change of the bar is simply the actual change in temperature at some intermediate point, so the above equation can also be written as:
This is the heat absorption equation.
Heat Equation
Equating the QΔt in the flux and absorption terms, we find the heat absorption equation to be:
If we divide the above equation by ΔxΔt and allow both Δx and Δt to both go to 0, we will obtain the heat conduction or diffusion equation:
where
and has the dimensions of length^2/time and called the thermal diffusivity
Boundary Conditions
Certain boundary conditions may apply to the specific heat conduction problem, for example: If one end is maintained at some constant
temperature value, then the boundary condition for that end is u = T.
If one end is perfectly insulated, then the boundary condition stipulates ux = 0.
Generalized Boundary Conditions Consider the end where x=0 and the rate of flow of
heat is proportional to the temperature at the end of the bar. Recall that the rate of flow will be given, from left to right, as
With this said, the rate of heat flow out of the bar from right to left will be
Therefore, the boundary condition at x=0 iswhere h1 is a proportionality constant
if h1=0, then it corresponds to an insulated endif h1 goes to infinity, then the end is held at 0
temp.
Generalized Boundary Conditions Similarly, if heat flow occurs at the end x = L, then the
boundary condition is as follows:
where, again, h2 is a nonzero proportionality factor
Initial Boundary Condition
Finally, the temperature distribution at one fixed instant – usually taken at t = 0, takes the form:
occurring throughout the bar
Generalizations
Sometimes, the thermal conductivity, density, specific heat, or area may change as the axial position changes. The rate of heat transfer under such conditions at x=x0 is now:
The heat equation then becomes a partial differential equation in the form:
or
Generalizations
Other ways for heat to enter or leave a bar must also be taken into consideration.
Assume G(x,t,u) is a rate per unit per time. Source
G(x,t,u) is added to the bar G(x,t,u) is positive, non-zero, linear, and u does not depend on t G(x,t,u) must be added to the left side of the heat equation
yielding the following differential equation
Generalizations
Similarly, Sink
G(x,t,u) is subtracted from the bar G(x,t,u) is positive, non-zero, linear, and u does not
depend on t G(x,t,u) then under this sink condition takes the
form:
Generalizations
Putting the source and sink equations together in the heat equation yields
which is commonly called the generalized heat conduction equation
Multi-dimensional space
Now consider a bar in which the temperature is a function of more than just the axial x-direction. Then the heat conduction equation can then be written: 2-D:
3-D:
Example 1: Section 10.6, Problem 9
Let an aluminum rod of length 20 cm be initially at the uniform temperature 25C. Suppose that at time t=0, the end x=0 is cooled to 0C while the end x=20 is heated to 60C, and both are thereafter maintained at those temperatures.
Find the temperature distribution in the rod at any time t
Example 1: Section 10.6, Problem 9Find the temperature distribution, u(x,t)
2uxx=ut, 0<x<20, t<0u(0,t)=0 u(20,t)=60, t<0u(x,0)=25, 0<x<20
From the initial equation we find that:L=20, T1=0, T2=60, f(x)=25
We look up the Thermal Diffusivity of aluminum→2=0.86
Example 1: Section 10.6, Problem 9Using Equations 16 and 17 found on page 614, we
find that
where
1112 sin, 2
222
n
Ltn
n LxnecT
LxTTtxu
L
n dxLxnT
LxTTxf
Lc
0 112 sin2
Example 1: Section 10.6, Problem 9Evaluating cn, we find that
nnc
nnnnnc
dxxnxc
n
n
L
n
50cos70
5sin12cos710
20sin0
2006025
202
2
0
Example 1: Section 10.6, Problem 9Now we can solve for u(x,t)
1
40086.0
1
2086.0
20sin50cos703,
20sin50cos700
20060,
2
2
222
n
tn
n
tn
xnennxtxu
xnennxtxu
Example 1: Section 10.6, Problem 9
Derivation of the Wave Equation
Applicable for:
• One space dimension, transverse vibrations on elastic string
• Endpoints at x = 0 and x = L along the x-axis
• Set in motion at t = 0 and then left undisturbed
Schematic of String in Tension
Equation DerivationSince there is no acceleration in the horizontal direction
However the vertical components must satisfy
where is the coordinate to the center of mass and the weight is neglected
Replacing T with V the and rearranging the equation becomes
0cos),()cos(),( txTtxxT
),(sin),()sin(),( txxutxTtxxT tt
x
),(),(),(
txux
txVtxxVtt
Derivation continued
Letting , the equation becomes
To express this in terms of only terms of u we note that
The resulting equation in terms of u is
and since H(t) is not dependant on x the resulting equation is
0x
),(),( txutxV ttx
),()(tan)(),( txutHtHtxV x
ttxx uHu )(
ttxx uHu
Derivation Continued
For small motions of the string, it is approximated that
using the substitution that
the wave equation takes its customary form of
TTH cos
/2 Ta
ttxx uua 2
Wave Equation Generalizations
The telegraph equation
where c and k are nonnegative constantscut arises from a viscous damping forceku arises from an elastic restoring forceF(x,t) arises from an external force
The differences between this telegraph equation and the customarywave equation are due to the consideration of internal elasticforces. This equation also governs flow of voltage or current in atransmission line, where the coefficients are related to the electricalparameters in the line.
),(2 txFuakucuu xxttt
Wave Equations in Additional DimensionsFor a vibrating system with more than on significant space
coordinate it may be necessary to consider the wave equation in more than one dimension.
For two dimensions the wave equation becomes
For three dimensions the wave equation becomes
ttyyxx uuua )(2
ttzzyyxx uuuua )(2
Example 2: Section 10.7, Problem 6Consider an elastic string of length L whose ends
are held fixed. The string is set in motion from its equilibrium position with an initial velocity g(x). Let L=10 and a=1. Find the string displacement for any time t.
,4,1
,4
LxL
Lx
xg
LxL
LxL
Lx
43
43
4
40
Example 2: Section 10.7, Problem 6From equations 35 and 36 on page 631, we find
that
where
1
sinsin,n
n Latn
Lxnktxu
L
n dxLxnxg
Lk
Lan
0sin2
Example 2: Section 10.7, Problem 6Solving for kn, we find:
4sin
43sin8
sin4
sin43sin42
sin4sinsin42
3
2
40
43
4 43
nnnaLk
nnnnL
ank
dxLxn
LxLdx
Lxndx
Lxn
Lx
Lk
Lan
n
n
L L
L
LLn
Example 2: Section 10.7, Problem 6Now we can solve for u(x,t)
133
133
13
10sin
10sin
4sin
43sin180,
sinsin4
sin43sin18,
sinsin4
sin43sin8,
n
n
n
tnxnnnn
txu
Latn
Lxnnn
nLtxu
Latn
Lxnnn
naLtxu
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