Abstract
We present an extension of the Stefan-type solution method applicable to multi-component, multi-phase 1D porous flows, and illustrate the method by applying it to phase separation dynamics in an NaCl–\(\hbox {H}_2\hbox {O}\)-saturated hydrothermal heat pipe. For this example, three mathematical models are constructed. The first two models concern the rate of progression of two interfaces, one separating brine from two-phase fluid and another separating two-phase fluid from single-phase liquid at seawater salinity. The brine layer model shows that the layer may reach quasi-steady-state thickness even while the salt content of the layer continues to increase; the two-phase layer model shows how variable heat flux at the top of the layer leads to departure from the linear growth rate predicted by a simpler model. The third model concerns the temperature profile in the entire column. The governing advection–diffusion equation has highly variable coefficients, with no negligible terms in it in the region of parameter space considered. We present a method to solve this type of equation by constructing a propagator and a corresponding Green’s function. Finally, we show how to use the developed framework to test the internal consistency of numerical simulations, again using the 1D heat pipe as an example.
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Abbreviations
- A :
-
Cross-sectional area (\(\hbox {m}^2\))
- C :
-
\(\frac{\tilde{\sigma }q y_{12}^2}{2A\rho _\mathrm{l} X_\mathrm{l}}\) (\(\hbox {m}^{-1}\,\hbox {s}^{-1}\))
- c :
-
Specific heat (\(\hbox {J}/\hbox {kg}\,^{\circ }\hbox {C}\))
- \(\mathcal {C}\) :
-
Content density [\(\hbox {(kg or J)}/\hbox {m}^3\)]
- \(\mathcal {F}\) :
-
Mass or heat flux [\(\hbox {(kg or J)}/\hbox {m}^2\,\hbox {s}\)]
- F :
-
\(-\mathcal {F}_0/\tilde{\lambda }\) (\({}^{\circ }\hbox {C}/\hbox {m}\))
- h :
-
Enthalpy (J/kg)
- I :
-
Layer energy or solute content (J or kg)
- \(\mathbb {N}\) :
-
\(\{0,1,2,...\}\) (dimensionless)
- Q :
-
Lateral salt loss (kg)
- q :
-
Proportionality constant [kg/(\(\hbox {m}^3\) s)]
- T :
-
Temperature (\({}^\circ \hbox {C}\))
- \(T_{ij}\) :
-
Temperature of interface between zones i and j (\({}^{\circ }\hbox {C}\))
- \(T_{\mathrm{H}}\) :
-
Top boundary temperature (\({}^\circ \hbox {C}\))
- t :
-
Time (s)
- v :
-
Darcy volumetric flux (m/s)
- X :
-
Bulk salinity (mass fraction)
- y :
-
Height (m)
- \(y_{ij}\) :
-
Position of interface between zones i and j (m)
- \(y_{12,\infty }\) :
-
Quasi-steady brine layer thickness (m)
- \(y_{\mathrm{H}}\) :
-
Height of the system (m)
- Y :
-
\(y-y_{23}\) (m)
- \(\alpha \) :
-
\(\frac{{\frac{\mathrm{d}}{\mathrm{d}t}}\langle \mathcal {C} \rangle }{(\langle \mathcal {C} \rangle - \mathcal {C}_{23})}\) (\(\hbox {s}^{-1}\))
- \(\beta \) :
-
\(\frac{\mathcal {F}}{(\langle \mathcal {C} \rangle - \mathcal {C}_{23})}\) (m/s)
- \(\gamma \) :
-
\(v_\mathrm{l} / \phi \) (m/s)
- \(\Delta x\) :
-
Width of pipe front (m)
- \(\Delta z\) :
-
Width of pipe side (m)
- \(\Delta \sigma \) :
-
Exposed surface area (\(\hbox {m}^2\))
- \(\epsilon \) :
-
\(C\gamma /\eta ^2\) (dimensionless)
- \(\zeta \) :
-
\(y/y_{23}\) (dimensionless)
- \(\eta \) :
-
\(\frac{1}{\xi }\langle \frac{\partial \xi }{\partial t} \rangle \) (\(\hbox {s}^{-1}\))
- \(\theta \) :
-
\(\theta _{\mathrm{I}}+\theta _{\mathrm{H}}=[T-T_{23}-F(y_{23}-y)]/Fy_{23}\) (dimensionless)
- \(\theta _{\mathrm{H}}\) :
-
Solution to homogeneous problem (dimensionless)
- \(\theta _{\mathrm{I}}\) :
-
Solution to inhomogeneous problem (dimensionless)
- \(\kappa \) :
-
Thermal diffusivity (\(\hbox {m}^2/\hbox {s}\))
- \(\tilde{\lambda }\) :
-
Medium thermal conductivity (\(\hbox {W}/\hbox {m}\,^{\circ }\hbox {C}\))
- \(\xi \) :
-
\(\rho X\) (\(\hbox {kg}/\hbox {m}^3\))
- \(\rho \) :
-
Bulk density (\(\hbox {kg}/\hbox {m}^3\))
- \(\tilde{\sigma }\) :
-
Pipe circumference (m)
- \(\tau \) :
-
\(\kappa t/y_{23}^2\) (dimensionless)
- \(\phi \) :
-
Porosity (dimensionless)
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Acknowledgements
We would like to thank R.P. Lowell and D. Scofield for fruitful discussions and for helpful comments on earlier versions of this manuscript as well as the reviewers for their thoroughness and insightful suggestions. Thanks also to the parents of K.C. Lewis for providing a peaceful working environment in the summer of 2016.
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Appendices
Appendix 1: Alternative Derivation of Equation (12)
The equations expressing the balance of salt or heat can both be cast in the form
where \(\mathcal {C}\) represents the content of salt or energy and \(\mathcal {F}\) represents combined advective and diffusive fluxes. Integrating both sides from the bottom to the top of the expansion layer gives
According to the Leibniz integral theorem,
Solving for the first term on the right-hand side and substituting the result into (89) gives
where \(\mathcal {C}_{ij}\equiv \mathcal {C}(y_{ij},t)\). Defining the average content density as in equation (10) and substituting into the above equation leads to equation (12).
Appendix 2: Derivation of the Stefan Condition
In the original Stefan problem that involves a half plane filled with melting ice, the position of the melt interface is found by imposing the Stefan condition [see (Carslaw and Jaeger 1959], pg. 284); in this section, we show how this condition may be derived from equation (12). Consider the upper half plane (\(y \ge 0\)) filled with ice and heated from below. In our notation, the Stefan condition reads
where the subscript 1 refers to liquid, the subscript 2 refers to ice, and L is the latent heat of fusion. In this scenario, equation (12) becomes
where \(\rho \) is the liquid density, h is the liquid enthalpy, and we have made the replacement \(\mathcal {C}=\rho h\). For simplicity, we have assumed that the liquid is raised only slightly above freezing so that variation of density within the liquid phase may be neglected. First, we note that the heat flux into the \(y_{12}\) interface from below is equal to the flux at the bottom boundary of the system minus the portion of that heat absorbed by the layer of liquid between the bottom boundary and \(y_{12}\); mathematically, this statement translates to
Second, we relabel the quantity \(\mathcal {F}_{12}\) as \(\mathcal {F}_{12,+}\), emphasizing that it is the flux of heat upward from \(y_{12}\). Making these replacements and setting
in equation (93) yields
Using Fourier’s law of heat conduction, we write
and
where both derivatives are evaluated at \(y_{12}\). Substituting these expressions into (96) gives equation (92).
In the problem of the receding ice sheet, the classical Stefan condition can be used to find the form of \(y_{12}(t)\) together with the temperature profile; however, this technique only works under very restricted conditions. For example, imposing a heat flux condition at the bottom boundary of the system instead of a constant temperature condition already leads to problems (see (Carslaw and Jaeger 1959)) for details). The generalized condition (12) avoids this difficulty by representing \(y_{ij}(t)\) as the solution of its own differential equation instead of as an auxiliary quantity to be determined simultaneously with T(y, t).
Appendix 3: Derivation of Condition (20)
Using the definitions
and
we find that
We seek the condition under which the second term on the right-hand side of (101) dominates the first and the third terms. The first and third terms are both of the order \(\dot{y}_{ij}\), while the second term is of order \(\kappa _i/y_{ij}\). Hence, the desired condition is that
which is identical with (20). This condition is sufficient but not necessary, because the first and third terms on the right-hand side of (101) are of opposite sign, and so may approximately cancel one another even if (102) is not satisfied.
Appendix 4: Derivation of Propagator and Green’s Function
To solve for \(\theta _{\mathrm{H}}(\zeta ,\tau )\) and construct the propagator, we begin by finding the eigenfunctions \(\psi _n(\zeta )\) and eigenvalues \(\lambda _n\) satisfying
where the eigenfunctions are required to satisfy the homogeneous boundary conditions (22) and (23). The solutions, normalized on the interval \(0 \le \zeta \le 1\), are
with
and \(n\in \mathbb {N}\). Now we search for a solution of the form
where the time-dependent coefficients \(a_n(\tau )\) are to be determined. Substituting (106) into (21), setting \(\tilde{f}(\zeta )=0\), and keeping in mind that the \(\psi _n\) satisfy (103), we obtain
The eigenfunctions are all linearly independent, so the only way the above equation can be satisfied is if each coefficient of \(\psi _n\) vanishes; the resulting differential equation in \(a_n(\tau )\) has the solution
where \(A_n\) is a constant for each n. Equation (106) now takes the form
It remains to choose the constants \(A_n\) so that the initial condition (24) is satisfied. Applying the initial condition to (109) gives
Multiplying both sides of this equation by \(\psi _m(\zeta )\), integrating from 0 to 1, and keeping in mind the orthonormality of the eigenfunctions results in
Changing m back to n, substituting the above expression into (109), and rearranging give the solution to the homogeneous problem as
The expression in brackets is the kernel of the desired integral operator, which propagates the solution at \(\tau = 0\) to that at a later time \(\tau \). Therefore, the kernel that propagates a solution at \(\tau =\tau '\) to a later time \(\tau \) is
It can be shown that multiplying the propagator with the Heaviside step function \(H(\tau -\tau ')\) produces the Green function required for solution of the associated inhomogeneous problem (see Bayin 2006); hence, the desired Green function is
The solution to the inhomogeneous problem is then
Carrying out the integral as far as possible with general \(\tilde{g}(\zeta ')\) results in
which is the same as equation (27). Using equation (24) and completing the integral in (112) yields
which is the same as equation (26). The full dimensionless solution \(\theta (\zeta ,\tau )\) is now given by (25).
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Lewis, K.C., Coakley, S. & Miele, S. An Extension of the Stefan-Type Solution Method Applicable to Multi-component, Multi-phase 1D Systems. Transp Porous Med 117, 415–441 (2017). https://doi.org/10.1007/s11242-017-0840-1
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DOI: https://doi.org/10.1007/s11242-017-0840-1