Porous medium equation

The porous medium equation, also called the nonlinear heat equation, is a nonlinear partial differential equation taking the form:[1]

u t = Δ ( u m ) , m > 1 {\displaystyle {\frac {\partial u}{\partial t}}=\Delta \left(u^{m}\right),\quad m>1}

where Δ {\displaystyle \Delta } is the Laplace operator. It may also be put into its equivalent divergence form: u t = [ D ( u ) u ] {\displaystyle {\partial u \over {\partial t}}=\nabla \cdot \left[D(u)\nabla u\right]} where D ( u ) = m u m 1 {\displaystyle D(u)=mu^{m-1}} may be interpreted as a diffusion coefficient and ( ) {\displaystyle \nabla \cdot (\cdot )} is the divergence operator.

Solutions

Despite being a nonlinear equation, the porous medium equation may be solved exactly using separation of variables or a similarity solution. However, the separation of variables solution is known to blow up to infinity at a finite time.[2]

Barenblatt-Kompaneets-Zeldovich similarity solution

The similarity approach to solving the porous medium equation was taken by Barenblatt[3] and Kompaneets/Zeldovich,[4] which for x R n {\displaystyle x\in \mathbb {R} ^{n}} was to find a solution satisfying: u ( t , x ) = 1 t α v ( x t β ) , t > 0 {\displaystyle u(t,x)={1 \over {t^{\alpha }}}v\left({x \over {t^{\beta }}}\right),\quad t>0} for some unknown function v {\displaystyle v} and unknown constants α , β {\displaystyle \alpha ,\beta } . The final solution to the porous medium equation under these scalings is: u ( t , x ) = 1 t α ( b m 1 2 m β x 2 t 2 β ) + 1 m 1 {\displaystyle u(t,x)={1 \over {t^{\alpha }}}\left(b-{m-1 \over {2m}}\beta {\|x\|^{2} \over {t^{2\beta }}}\right)_{+}^{1 \over {m-1}}} where 2 {\displaystyle \|\cdot \|^{2}} is the 2 {\displaystyle \ell ^{2}} -norm, ( ) + {\displaystyle (\cdot )_{+}} is the positive part, and the coefficients are given by: α = n n ( m 1 ) + 2 , β = 1 n ( m 1 ) + 2 {\displaystyle \alpha ={n \over {n(m-1)+2}},\quad \beta ={1 \over {n(m-1)+2}}}

Applications

The porous medium equation has been found to have a number of applications in gas flow, heat transfer, and groundwater flow.[5]

Gas flow

The porous medium equation name originates from its use in describing the flow of an ideal gas in a homogeneous porous medium.[6] We require three equations to completely specify the medium's density ρ {\displaystyle \rho } , flow velocity field v {\displaystyle {\bf {v}}} , and pressure p {\displaystyle p} : the continuity equation for conservation of mass; Darcy's law for flow in a porous medium; and the ideal gas equation of state. These equations are summarized below: ε ρ t = ( ρ v ) ( Conservation of mass ) v = k μ p ( Darcy's law ) p = p 0 ρ γ ( Equation of state ) {\displaystyle {\begin{aligned}\varepsilon {\partial \rho \over {\partial t}}&=-\nabla \cdot (\rho {\bf {v}})&({\text{Conservation of mass}})\\{\bf {v}}&=-{k \over {\mu }}\nabla p&({\text{Darcy's law}})\\p&=p_{0}\rho ^{\gamma }&({\text{Equation of state}})\end{aligned}}} where ε {\displaystyle \varepsilon } is the porosity, k {\displaystyle k} is the permeability of the medium, μ {\displaystyle \mu } is the dynamic viscosity, and γ {\displaystyle \gamma } is the polytropic exponent (equal to the heat capacity ratio for isentropic processes). Assuming constant porosity, permeability, and dynamic viscosity, the partial differential equation for the density is: ρ t = c Δ ( ρ m ) {\displaystyle {\partial \rho \over {\partial t}}=c\Delta \left(\rho ^{m}\right)} where m = γ + 1 {\displaystyle m=\gamma +1} and c = γ k p 0 / ( γ + 1 ) ε μ {\displaystyle c=\gamma kp_{0}/(\gamma +1)\varepsilon \mu } .

Heat transfer

Using Fourier's law of heat conduction, the general equation for temperature change in a medium through conduction is: ρ c p T t = ( κ T ) {\displaystyle \rho c_{p}{\partial T \over {\partial t}}=\nabla \cdot (\kappa \nabla T)} where ρ {\displaystyle \rho } is the medium's density, c p {\displaystyle c_{p}} is the heat capacity at constant pressure, and κ {\displaystyle \kappa } is the thermal conductivity. If the thermal conductivity depends on temperature according to the power law: κ = α T n {\displaystyle \kappa =\alpha T^{n}} Then the heat transfer equation may be written as the porous medium equation: T t = λ Δ ( T m ) {\displaystyle {\partial T \over {\partial t}}=\lambda \Delta \left(T^{m}\right)} with m = n + 1 {\displaystyle m=n+1} and λ = α / ρ c p m {\displaystyle \lambda =\alpha /\rho c_{p}m} . The thermal conductivity of high-temperature plasmas seems to follow a power law.[7]

See also

References

  1. ^ Wathen, A; Qian, L. "Porous medium equation" (PDF). University of Oxford.
  2. ^ Evans, Lawrence C. (2010). Partial Differential Equations. Graduate Studies in Mathematics. Vol. 19 (2nd ed.). American Mathematical Society. pp. 170–171. ISBN 9780821849743.
  3. ^ Barenblatt, G.I. (1952). "On some unsteady fluid and gas motions in a porous medium". Prikladnaya Matematika i Mekhanika (in Russian). 10 (1): 67–78.
  4. ^ Zeldovich, Y.B.; Kompaneets, A.S. (1950). "Towards a theory of heat conduction with thermal conductivity depending on the temperature". Collection of Papers Dedicated to 70th Anniversary of A. F. Ioffe. Izd. Akad. Nauk SSSR: 61–72.
  5. ^ Boussinesq, J. (1904). "Recherches théoriques sur l'écoulement des nappes d'eau infiltrées dans le sol et sur le débit des sources". Journal de Mathématiques Pures et Appliquées. 10: 5–78.
  6. ^ Muskat, M. (1937). The Flow of Homogeneous Fluids Through Porous Media. New York: McGraw-Hill. ISBN 9780934634168.
  7. ^ Zeldovich, Y.B.; Raizer, Y.P. (1966). Physics of Shock Waves and High Temperature Hydrodynamic Phenomena (1st ed.). Academic Press. pp. 652–684. ISBN 9780127787015.
  • The Porous Medium Equation: Mathematical theory