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Citation:
Schaffranek, R.W., 1998, Simulation Model for Open-Channel Flow and
Transport, in Proceedings of the First Federal Interagency Hydrologic
Modeling Conference, April 19-23, 1998, Las Vegas, NV: Subcommittee on
Hydrology of the Interagency Advisory Committee on Water Data, p. 1-103 to
1-110.
Abstract
Introduction
Unsteady Flow Equations
Four-Point Implicit Solution
Transport Simulation Component
Transport Solution
The Tidal Potomac River
Model Implementation
Numerical Simulation Results
Particle Tracking
Constituent Transport
Summary and Conclusions
References
In the effort described herein, the Lagrangian particle-tracking scheme of the dynamic flow model has been extended to include full solution of the transport equation by incorporating treatment of the physical process of dispersion. This direct coupling of the unsteady-flow and transport solutions eliminates the errors of numerical dispersion inherently introduced in de-coupled approaches wherein flow velocities must be interpolated to comply with the grid-point requirements of the transport scheme. Moreover, a coupled flow/transport simulation approach is required in situations where the fluid density varies longitudinally---as typically encountered in tidal-influenced, sediment-laden, or thermally-varying riverine flows---necessitating treatment of pressure differentials in the unsteady-flow equations.
In this paper, the BRANCH model of the tidal Potomac River network (Schaffranek 1987b) is used to demonstrate the coupled flow/transport simulation capability of the generic model. A previous numerical simulation, based on tracking parcels of water representing a conservative, non-dispersive constituent (Schaffranek 1987b), is repeated and revised to illustrate the capabilities of the model in simulating the combined effects of advection and dispersion on solute transport. Numerical simulations, conducted at varied Peclet numbers, illustrate the stability of the method when advection is the dominant process and the controlled response of the method for representation of physical dispersion without the introduction of numerical artifacts.
(2)
,
A, g, Sf,
,
, and
Vw, represent the channel top width, lateral inflow per
unit length of channel, the Boussinesq momentum-correction coefficient, the
cross-sectional area, gravitational acceleration, the friction slope, the
x-component of lateral-inflow velocity, the wind-stress coefficient,
and the wind velocity (occurring at an angle
to the longitudinal axis of the channel), respectively. The
momentum coefficient,
, defined
as
u2dA/U2A, in which u
is the velocity of water flowing through some finite elemental area dA
and U is the mean flow velocity in the cross-sectional area A,
is used to adjust for any nonuniform velocity distribution in the channel
cross section. A Manning formulation of the friction-slope term is used in
which Sf takes the form (
/
)2Q |Q|
/A2R4/3, wherein
= 1.0 for metric or 1.486 for
foot-pound units, R is hydraulic radius, and the symbol
is used in place of the Manning n
to indicate that the coefficient is being used to represent frictional
resistance under unsteady-flow conditions. The dimensionless wind-stress
coefficient,
, is a function of the
water-surface drag coefficient, Cd, the water density,
, and atmospheric density,
, expressed as Cd(
/
).
. The
finite-difference approximation of the spatial derivatives can vary from
box-centered (
= 0.5) to fully
forward (
= 1), which is the
range for which its stability has been proven. See, for example, Fread
(1974) for stability analysis using a linear wave approximation with a
linearized form of the friction-slope term, and Samuels and Skeels (1990) for
Fourier stability analysis of the linearized numerical equations including
the general form of the friction term. To avoid computational-mode
oscillations, a practical lower limit for
appears to be 0.6 (Schaffranek et al. 1981). Time
derivatives are centered in space; geometric properties and functional
quantities are centered in space and time weighted according to
. After the flow equations are
coupled recursively to eliminate internal nodes, the matrix of flow and
boundary-condition equations is solved in iterative fashion by Gaussian
elimination using maximum pivot strategy.
)
is resolved by tracking particles representing parcels of water in a
Lagrangian reference frame, whereas the dispersion process (
) is solved in a Eulerian framework
by a finite-difference technique. A cubic spline is employed to interpolate
the concentration profile of advected particles. An explicit, space-centered
finite-difference scheme is used to represent the dispersion process. This
solution approach avoids the well-known difficulties associated with
numerical dispersion in advection-dominated systems introduced by pure
Eulerian finite-difference solution methods. (See, for example, Gray and
Pinder (1976).)The cubic spline interpolant for the concentration profile is based on the method developed by Akima (1978). This spline interpolation technique has the desirable feature of minimizing the development of oscillations manifested as over- and under-shoot in the interpolated function. The Akima spline attempts to preserve the shape of the concentration profile as reflected by the data. The behavior of the Akima spline method is compared with a natural cubic spline (de Boor 1978) interpolation of the same function, potentially representative of a temporal or spatial constituent concentration profile, in Fig. 1. Endpoint conditions are automatically determined by the Akima method, whereas values of zero are specified for second derivatives at the endpoints for the natural spline. The extraneous inflection points of the natural cubic spline (Fig. 1a), yielding over- and under-shoot in the interpolated function, are clearly illustrated in contrast to the smoother interpolant produced by the Akima spline method (Fig. 1b). Moreover, the Akima spline reduces the potential for the generation of negative concentrations as is evidenced in the interpolation produced by the natural spline (Fig. 1a). These attributes of the Akima spline interpolation method contribute to improved conservation properties for the transport-solution technique.
(fig. 1a)
(fig. 1b)
Boundary conditions used to conduct numerical simulations include zero
discharges at the ends of tributaries and inlets, tide elevations recorded at
Indian Head, and freshwater inflows derived from a rated gaging station near
the head-of-tide. Freshwater inflows at the head-of-tide average 323
m3/s, but have ranged from 3 to 13,700 m3/s. Tidal
amplitude at Indian Head is about 55 cm, but wind effects can significantly
dampen tidal propagation. Wind speed and direction data collected at Indian
Head are used to evaluate wind-forcing effects. Flow simulations are
conducted using a 15-minute time step, which yields a Courant number
Cr
6.
The model was calibrated and verified using five sets of tidal-cycle flow
discharges measured at three different locations within the tidal-river
system. Measured and model-computed flood and ebb flow volumes agree within
10 percent (Schaffranek 1987b).
Particle Tracking: The transport of a conservative-type substance by advective processes alone is illustrated by the simulation results presented in Fig. 2. These results were obtained by tracking index particles representing parcels of water. In the simulation, nine index particles---potentially representing the location of a conservative, neutrally buoyant, passive solute or suspended particulate matter---were tracked through the main channel of the tidal river. The paths of travel of these particles are shown in the central graph of the figure. The vertical axis of the time-of-travel graph represents the main tidal Potomac River channel between Chain Bridge and Indian Head. The upper hydrograph in the figure shows the freshwater inflow recorded near Chain Bridge and lower hydrograph presents the tidal water-surface elevations simultaneously recorded at Indian Head. Together these hydrographs constitute the instantaneous boundary conditions used to solve the unsteady-flow equations.

The simulation results plotted in Fig. 2 demonstrate the combined effects of freshwater inflows and tidal forcing on the displacement of index particles and give indications of the retention properties and flushing characteristics of the tidal-river system. Throughout the period, the movement of index particles is variously influenced by the predominately semi-diurnal tides at Indian Head as they cycle through spring-neap variations and changing freshwater inflows at the head-of-tide. Near the end of the period, increased freshwater inflows, declining tidal elevations, and a significant wind event act to produce a pronounced downstream particle displacement. As is evident from the particle tracks, there is a tendency throughout the period for all particles to move closer to one another as they are advected along the channel. This variability in particle displacement can be attributed to the dynamic flow conditions and, in particular, to the magnitude and resultant dominance of the net tidal influx into the system as compared with the magnitude of freshwater inflows. This tidal dominance yields extended periods of little or no net downstream, and occasionally upstream, displacement of particles, which contributes to a diminished flushing capacity.
Constituent Transport:
The transport of a conservative, non-reactive constituent along the tidal
Potomac River, under the influences of both advection and longitudinal
dispersion, is illustrated in Fig. 3. The results of four transport
simulations are presented in Fig. 3b for the initial, hypothetical,
constituent concentration profile presented in Fig. 3a. The transport
simulation is for the same conditions as used to generate the
particle-tracking results presented in Fig. 2. Distances on the horizontal
axis of the figure are referenced to Chain Bridge. The four concentration
profiles of a transported constituent, illustrated in Fig. 3b, present
simulation results midway through the 30-day period at midnight on August
29. Values of 0, 1, 5, and 10 m2/s were assigned to the
dispersion coefficient, Dx. These coefficient values
represent pure advection, Dx = 0, and mixed
advection-dispersion conditions, Dx = 1, 5, 10, identified
by Peclet numbers, Pe = (
), of 20, 4, and 2, respectively, for the mean flow velocity
and 800 m grid-point spacing,
x, of particles.
(fig. 3a)
(fig. 3b)
As Fig. 3 illustrates, the transport solution of the model yields stability in all four numerical simulations. In particular, no instabilities are visible and no numerical dispersion is evident in the simulation results in which pure advection is considered. The simulations, in which dispersive transport is also evaluated, i.e., Dx = 1, 5, 10 m2/s, illustrate that the attendant spreading of the concentration profiles can contribute to a lengthening of the retention time for a constituent within the system. Thus, the compression of the concentration profile as demonstrated in the pure advection results of the particle-tracking simulation will be diminished, and potentially overwhelmed, by the process of physical dispersion with resultant consequences on the evaluation of transport of a constituent through the system. By full consideration of advection and dispersion transport processes such as this, a more comprehensive analysis of the flushing capacity and retention properties of the tidal-river network can be conducted. This will lead to more definitive evaluations of the fate and resultant effects of constituents, potentially introduced or naturally occurring, within the system.
de Boor, C. (1978). A practical Guide to Splines: Springer-Verlag, New York, N.Y., 392 p.
Fread, D.L. (1974). Numerical properties of implicit four-point finite difference equations of unsteady flow: Technical Memorandum NWS HYDRO-18, U. S. National Oceanic and Atmospheric Admin., Silver Spring, Md., 38 p.
Gray, W.G., and Pinder, G.F. (1976). An analysis of the numerical solution of the transport equation: Water Resources Research, 12(3), 547-555.
Lai, C. (1986). Numerical modeling of unsteady open-channel flow: Advances in Hydroscience, V.T. Chow and B.C. Yen, eds., Vol. 14, Academic Press, Orlando, Fla., 163-333.
Preissmann, A. (1961). Propagation of translatory waves in channels and rivers; (in French), Proc., First Congress of French Association for Computation (AFCAL), Grenoble, France, 433-442.
Samuels, P.G., and Skeels, C.P. (1990). Stability limits for Preissmann's scheme: ASCE Journal of Hydraulic Engineering, 116(8), 997-1012.
Schaffranek, R.W. (1987a). Flow model for open-channel reach or network: Professional Paper 1384, U.S. Geological Survey, Denver, Colo., 11 p.
Schaffranek, R.W. (1987b). A flow-simulation model of the tidal Potomac River. Water-Supply Paper 2234-D, U.S. Geological Survey, Denver, Colo., 41 p.
Schaffranek, R.W., Baltzer, R.A., and Goldberg, D.E. (1981). A model for simulation of flow in singular and interconnected channels: Book 7, Chap. C3, Techniques of Water Resources Investigations, U.S. Geological Survey, Denver, Colo., 110 p.
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