phil ess
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Homework Statement
I have been asked to model the flow of a slightly compressible liquid through a rigid, incompressible porous medium in 1D, assuming the flow obeys Darcy's law. I am given a rectangular prism of cross sectional area A with length L, a source of liquid (say water) on one side with total discharge Q, along with variables concerning the properties of the medium (porosity, permeability, etc). I am ignoring dispersion and diffusion effects.
Basically I am looking to find the pressure in the tube as a function of position and time, P(x,t).
Homework Equations
The Attempt at a Solution
Combining the continuity equation,
\epsilon\frac{\partial\rho}{\partial t} + \nabla\cdot\left(\rho k \nabla v\right) = 0
Ignore above line, not showing up correctly,
\epsilon\frac{\partial\rho}{\partial t} + \nabla\cdot\left(\rho k \nabla v\right) = 0
with Darcy's law,
v = \frac{-k}{\mu}\nabla P
we get,
\epsilon\mu\frac{\partial\rho}{\partial t} = \nabla\cdot\left(\rho k \nabla P\right)
Then assuming a liquid with compressibility c,
\rho = \rho_{o}e^{c(P-P_{o}}
which combines with the above to give the governing equation:
\epsilon\mu c \frac{\partial P}{\partial t} = \nabla\cdot\left(k \nabla P\right)
Combining the constant terms together, and since we are only considering the 1D flow in the x direction:
\frac{\partial P}{\partial t} = \alpha\frac{\partial^{2}P}{\partial x^{2}}
*** The first few equations are not showing up correctly. But what is important is the final results which seem ok.
Now all I need to do is solve this equation to get P(x,t).
What I am having problems with is the boundary conditions. I haven't taken any PDE courses or anything, so I'm not sure how they are supposed to be formulated, but I'll give some guesses:
P(x,0) = Pi ie. the pressure initially is some constant throughout the medium
Q = constant ie. the input flow rate is constant for all t
P(L,inf) = ?
I am assuming a finite medium with no discharge, so the liquid, and the pressure, will build up indefinitely, but I don't know what to put for the boundary at the end.
Like I said I am unfamiliar with PDEs which makes this very difficult. Later this problem will be extended to multi-phase flow, but this was given as a warm up for now.
Any help with this problem would be greatly appreciated! Thank you!