Multidimensional Numerical Dispersion

1983 ◽  
Vol 23 (01) ◽  
pp. 143-151 ◽  
Author(s):  
John R. Fanchi

Abstract Numerical dispersion can cause a smearing of otherwise sharp saturation fronts. The usual methods of estimating the magnitude of the smearing effect in one dimension (1D) are shown to apply in two and three dimensions (2 and 3D) as well. Besides the smearing effect, numerical dispersion affects the finite-difference solution of a multidimensional flow problem by rotating the principal flow axes. A method for determining the importance of the rotation effect is discussed. Numerical illustrations are included. Introduction Most reservoir simulation models available today obtain solutions to fluid flow equations-usually nonlinear partial differential equations-by replacing derivatives with finite-difference approximations. The use of these approximations, derived by manipulating Taylor's series, introduces an error known as truncation error. For many problems, the error is small and the approximate solutions of the subsequent finite-difference equations are sufficiently accurate for engineering purposes. However, truncation error can cause significant solution inaccuracies for certain types of problems. Examples of these problems include miscible floods and immiscible floods in which viscous forces are much larger than capillary forces. The most common example of the latter is the Buckley-Leverett problem with capillary pressure set to zero. A relatively simple equation that exhibits the effect of truncation error is the 1D convection-dispersion equation, (1) where the constant coefficients phi, K, and v are porosity, the dispersion coefficient, and velocity, respectively. The solution, S, of Eq. 1 may be saturation or concentration. The finite-difference solution of Eq. 1 introduces truncation error that can smear an otherwise sharp saturation front as if additional physical dispersion were present. This smearing, caused by truncating Taylor's series, often is called numerical dispersion or numerical diffusion. Truncation error studies often begin with a 1D convection-dispersion equation, such as Eq. 1, after the space and time coordinates (x and t) are redefined to remove two of the three constant coefficients (phi, K, and v). It appears that the effects of numerical dispersion in more than 1D have not been studied analytically, though attempts to minimize numerical dispersion in 2D -- particularly the grid orientation effect -- are numerous. All the attempts in more than 1D are empirical in the sense that the degree of success of the proposed numerical dispersion reduction method is determined relative to a case that does not include the proposed method. It is the purpose of this paper to present an analysis of the effects of numerical dispersion on the finite-difference numerical solution of the multidimensional convection-dispersion equation. The analytic results will provide a better understanding of the role that numerical dispersion plays in 2- or 3D; they can be used for estimating numerical dispersion effects, and they can provide a standard analytic basis for evaluating the degree of success of proposed numerical dispersion reduction methods. Analytical expressions for multidimensional numerical dispersion (MND) coefficients, derived by performing a truncation error analysis on the 3D convection-dispersion equation, are presented. This analysis is analogous to that used by Lantz in 1D. The significance of the results then is examined. SPEJ P. 143^

1982 ◽  
Vol 22 (03) ◽  
pp. 399-408 ◽  
Author(s):  
R.G. Larson

Abstract The one-dimensional (1D) material balance equations for multiphase multicomponent transport in porous media can be cast into forms, analogous to characteristic equations, that express explicitly the velocities at which fixed values of concentration are propagated. Use of these concentration-velocity equations to control the frequency with which component fluxes from finite-difference gridblocks ate updated leads to greatly reduced numerical dispersion, as demonstrated in miscible flooding, waterflooding, surfactant flooding, and other example problems. Introduction Accurate numerical simulation of enhanced oil-recovery processes, such as CO2, surfactant, thermal, or caustic flooding can involve calculations of phase behavior, interfacial tension, relative permeabilities, viscosities, heat and mass transfer, and even chemical reactions, thereby requiring considerable computational effort for each meshpoint or gridblock at each timestep. It is therefore impractical to resolve the steep concentration or thermal gradients often present in these processes by resorting to ultrafine meshes. Because the mathematical description of such processes is often unavoidably complex, it is important that the numerical technique be simple and ruggedly insensitive to the details of the process description, if one is to avoid becoming ensnarled in cumbersome and tedious programming and debugging.Although the finite-difference method's simplicity is its great advantage, its accuracy is seriously deficient, at least when one is using the simplest and most obvious discretizations. Central-difference discretization leads to artificial oscillations and overshoot, and upstream differencing leads to artificial smearing of sharp fronts-i.e., numerical dispersion or truncation error. Upstream difference solutions in two or three dimensions often show a significant dependence on grid orientation. Suggested improvements in the finite-difference technique, such as "transfer of overshoot," "truncation error analysis," or "two-point upstream weighting," still have significant numerical dispersion, grid orientation or oscillation errors.The method of characteristics, or point tracking, incurs no numerical dispersion or overshoot errors, but for general multicomponent, multidimensional problems, computer programs based on these techniques can become labyrinthine in their complexity.The finite-element, or variational, methods hold the potential of significantly reducing overshoot and/or numerical dispersion below that produced by finite difference, but implementation is considerably more complicated and time-consuming.The method of random choice, a technique developed for solving sets of multidimensional hyperbolic equations that appear in gas dynamics, recently has been employed in reservoir simulation. This method is somewhat akin to point tracking, propagating discontinuous fronts without smearing or overshoot errors.A new numerical technique is presented here that has the form and simplicity of finite difference, but utilizes variably timed flux updating (VTU) to gain a considerable improvement in accuracy. The technique is potentially applicable to general multicomponent, multidimensional problems. In this and a companion paper (see Pages 409-419), however, the technique is restricted to problems governed by the following equations. SPEJ P. 399^


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