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Advection diffusion equation

In the second model, the distribution and removal rates of tracers in the ocean are characterized through a one dimensional, (vertical) diffusion-advection equation. In this model, which ignores all horizontal processes, the equation governing the distribution of tracer in the soluble phase is [51,52,53,54] ... [Pg.368]

This study has shown that the application of EO can move TCE from a contaminated zone across an intact column of tight soil. The output from a ID diffusion-advection equation agrees well with the observed TCE concentration profiles, indicating that the transport equation is an appropriate model. [Pg.111]

Stute et al. (1992) made numerical calculation to study flow dynamics of the Great Hungarian Plain (GHP) aquifer system with the use of He concentration data. They solved the diffusion-advection equation for He transport for a two-dimensional case. [Pg.139]

Consider the binary chemical reaction A + B —> C. The reaction-diffusion-advection equations read, in the case of equal diffusion co-... [Pg.152]

In the case of the fast binary reaction we could eliminate the reaction term from the reaction-diffusion-advection equation. But in general this is not possible. In this chapter we consider another class of chemical and biological activity for which some explicit analysis is still feasible. We consider the case in which the local-reaction dynamics has a unique stable steady state at every point in space. If this steady state concentration was the same everywhere, then it would be a trivial spatially uniform solution of the full reaction-diffusion-advection problem. However, when the local chemical equilibrium is not uniform in space, due to an imposed external inhomogeneity, the competition between the chemical and transport dynamics may lead to a complex spatial structure of the concentration field. As we will see in this chapter, for this class of chemical or biological systems the dominant processes that determine the main characteristics of the solutions are the advection and the reaction dynamics, while diffusion does not play a major role in the large Peclet number limit considered here. Thus diffusion can be neglected in a first approximation. [Pg.164]

In the previous chapters we discussed various aspects of chemical and biological activity in fluid flows presenting certain classes of dynamical behavior that can be described by reaction-diffusion-advection equations and analyzed using dynamical systems approaches. However, there are many research areas of chemical or biological processes taking place in fluid environments that were not covered in the previous chapters. Here we briefly discuss some of these areas and point the reader to the relevant literature for further reading. Apart from classical well-studied topics, here we also focus on more recent developments and active areas of current research. [Pg.247]

We use Model C, given by (5.27), for the mean-field equation for p x,t) with z) = (p(t)w z). The standard diffusion approximation of (5.27), i.e., taking the limit of small jump lengths and small waiting times, yields the reaction-diffusion-advection equation... [Pg.175]

The concentration profile c(x, y, z, i) of a passive tracer under these flow conditions can be determined using the diffusion-advection equation given below ... [Pg.1316]

The conservation of species is actually the law of conservation of mass applied to each species in a mixture of various species. The fluid element, as described in Sections 6.2.1.1 through 6.2.1.3, does not comprise of pure fluid with only one species, such as water, but of many species forming a multicomponent mixture. This law is mathematically described by the continuity equation for species, also known as the species equation, advection-diffusion equation, or convection-diffusion equation. If the species equation additionally includes a reaction term, it is known as the reaction-diffusion-advection equation. [Pg.213]

Yaimacopoulos, A.N., Tomlin, A.S., Brindley, J., Merkin, J.H., Pilling, MJ. Error propagation in approximations to reaction-diffusion-advection equations. Phys. Lett. A 223, 82-90 (1996b) Yarwood, G., Rao, S., Yocke, M., Whitten, G. Updates to the Carbon Bimd chemical mechanism CB05. Final Report to the US EPA, RT-0400675 (2005)... [Pg.312]

Consider the instantaneous release of a fixed mass of material, Q, into an infinite expanse of air (a ground surface will be added later). The coordinate system is fixed at the source. Assuming no reaction or molecular diffusion, the concentration C of material resulting from this release is given by the advection equation... [Pg.177]

Solving the purely advective equation or even introducing an advection term into the diffusion equation is a source of numerical difficulties. The simplest advection equation of a medium moving at velocity v in one dimension can be written... [Pg.165]

As we saw with the steady-state water-column application of the one-dimensional advection-diffusion-reaction equation (Eq. 4.14), the basic shapes of the vertical concentration profiles can be predicted from the relative rates of the chemical and physical processes. Figure 4.21 provided examples of profiles that exhibit curvatures whose shapes reflected differences in the direction and relative rates of these processes. Some generalized scenarios for sedimentary pore water profiles are presented in Figure 12.7 for the most commonly observed shapes. [Pg.309]

Transport Processes and Gauss Theorem One-Dimensional Diffusion/Advection/Reaction Equation Box 22.1 One-Dimensional Diffusion/Advection/Reaction Equation at Steady-State... [Pg.1005]

Table 22.2 Solution of Diffusion/Advection/Reaction Equation at Steady-State A, and A2 of Eq. 22-9 for Different Types of Boundary Conditions... Table 22.2 Solution of Diffusion/Advection/Reaction Equation at Steady-State A, and A2 of Eq. 22-9 for Different Types of Boundary Conditions...
The one-dimensional diffusion/advection/reaction equation at steady-state is (22-7) ... [Pg.1010]

Situations in which either Da or Pe are much larger or much smaller than 1 indicate that in the diffusion-advection-reaction equation some of these processes are dominant while others can be disregarded. Figure 22.3 gives an overview of such cases. A first distinction is made according to the size of Da ... [Pg.1013]

The model (Fig. 23.6) consists of three compartments, (a) the surface mixed water layer (SMWL) or epilimnion, (b) the remaining open water column (OP), and (c) the surface mixed sediment layer (SMSL). SMWL and OP are assumed to be completely mixed their mass balance equations correspond to the expressions derived in Box 23.1, although the different terms are not necessarily linear. The open water column is modeled as a spatially continuous system described by a diffusion/advection/ reaction... [Pg.1085]

Section 3.2 introduced the governing equations for three physical processes responsible for transporting material in living systems advection, drift, and diffusion. Advection refers to the process by which solutes are transported with the bulk... [Pg.195]

We consider the case of a unique scalar reactive field 0(jc, t). This model is appropriate in aqueous autocatalytic premixed reactions, as well as in gaseous combustion with a large flow intensity but low value of gas expansion across the flame [7]. The field 0 evolves according to the advection-reaction-diffusion (ARD) equation ... [Pg.530]

The truncation error associated with convection/advection schemes can be analyzed by using the modified equation method [205]. By use of Taylor series all the time derivatives except the 1. order one are replaced by space derivatives. When the modified equation is compared with the basic advection equation, the right-hand side can be recognized as the error. The presence of Ax in the leading error term indicate the order of accuracy of the scheme. The even-ordered derivatives in the error represent the diffusion error, while the odd-ordered derivatives represent the dispersion (or phase speed) error. [Pg.1025]

Equation 2.20 is the advection-dispersion (AD) equation. In the petroleum literature, the term convection-diffusion (CD) equation is used, or simply diffusion equation (Brigham, 1974). When a reaction term is included, the term advection-reaction-dispersion (ARD) equation is used elsewhere. When the adsorption term is expressed as a reaction term, the ARD equation is as discussed later in Section 2.4. Several solutions of Eq. 2.20 have been presented in the literature, depending on the boundary conditions imposed. In general, they are various combinations of the error function. When the porous medium is long compared with the length of the mixed zone, they all give virtually identical results. [Pg.18]

Imboden and Schwarzenbach (1985) have illustrated how the mass-balance equation is a means of accounting for chemical and biological reactions that produce or consume a chemical within a test volume, and for transport processes dial import or export the chemical across the boundaries. Each process acting on a chemical can be characterized by an environmental first-order rate constant, expressed in units of time-1. Transport mechanisms include water renewal by nvers, horizontal and vertical turbulent diffusion, advection by lake particles, and settling of particles (Imboden and Schwarzenbach, 1985). Chemical reaction i ales and reaction half-lives for a wide variety of reactions have been summarized by I loffmann (1981), Pankow and Morgan(1981), Morgan and Stone(1985),and Santsehi (1988). [Pg.22]

Same depths, eddy diffusion coefficient, and ad-vection as in Figure 12. Solid curves eddy diffusion, advection, and radioactive decay. Equations 52, 59. Dashed curves eddy diffusion, advection, decay, and production. Equation 62. [Pg.71]

This interpretation of the effective diffusion in terms of individual trajectories of an ensemble of particles advected by the flow and a superimposed random Brownian motion, as described by the stochastic advection equation (2.34), can be extended further. The characteristic time for molecular diffusion across the channel td L2/D gives the correlation time of the longitudinal velocity experienced by a particle. Thus the longitudinal motion can be described as a collection of independent longitudinal displacements of typical length Utd over time intervals td- Thus, for long times, t td, the effective diffusion coefficient of such random walk can be estimated as Deff (Utd)2/td U2L2/D that is consistent with (2.51) when Pe > 1. [Pg.38]

In a reaction-diffusion-advection formulation, the model considers a one-dimensional slice transverse to concentration filaments, and models its evolution by an equation of the type... [Pg.152]

Movement and fate of radionuclides in groundwater follow the transport components represented by the basic diffusion/dispersion-advection equation. The following expression describes the basic equation for the advective and dispersive transport with radioactive decay and retardation for the radionuclide transport in the groundwater ... [Pg.472]

To illustrate the importance of the definition of the deterministic and stochastic velocity components 5, and let us suppose a puff of species of known concentration distribution c(x, o) at time to- In the absence of chemical reaction and other sources, and assuming molecular diffusion to be negligible, the concentration distribution at some later time is described by the following advection equation ... [Pg.829]

The solute flow process includes advection (or convection), dispersion and diffusion. The equation for the process can be written as... [Pg.583]


See other pages where Advection diffusion equation is mentioned: [Pg.381]    [Pg.413]    [Pg.266]    [Pg.1007]    [Pg.155]    [Pg.202]    [Pg.650]    [Pg.280]    [Pg.188]    [Pg.1043]    [Pg.169]    [Pg.381]    [Pg.1115]    [Pg.207]    [Pg.655]   
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