p/
t = D
2p/
x2 -
u
p/
x
a). where D is a constant. We can write down a general solution describing how it will disperse , but we need to specialise to our specific case to get a physical applicable answer.
Remember the tubes were sealed at both ends ; this means the
flow substance at either end of the tube has to be zero. It turns
out this is proportional to the first derivative, xc
of the concentration. So we would like this to be zero at the both
ends.
c/
x
x=0x =
0,
c/
x
x=L =
0.
In this case it is of the form , c(x,0) ~ (x) since we
injectb all point. A condition which a quantity that varies
throughout a given space or enclosure must fulfill at every point
on the boundary of that space especially when the velocity of a
fluid at any point on the wall a rigid conduit is necessary
parallel to the wall. For example, if the independent variable is
time over the domain [0,1], a boundary value problem would specify
values fpr y(t) at both t = 0 and t=1 , whereas an initial value
problem would specify a vlaue of y(t) and y'(t) at time t = 0.
b). In other words it makes some sense that we should expect
that as t our
tempratue distribution, u (x,t) should behaves as,
u (x,t) = uE (x)
where, uE (x) is called the equilibium temperature.
Note as well that is should still satisfy the heat equation and
boundary conditons. It would not satisfy the initial condition
however because it is the temperature distribution as t
whereas the initial condition is at t = 0. So, the eqilibirium
temperature distribution should satisfy,
0 = d2uE/dx2 uE (0) = T1 uE (L) = T2
This is a really ordinary differential equation. If we integrate twice we get
uE = (x) = c1x + c2
and applying Boundary condition
uE(x) = T1 + (T2 - T1)x/L.
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