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Models differential equations governing

In most adsorption processes the adsorbent is contacted with fluid in a packed bed. An understanding of the dynamic behavior of such systems is therefore needed for rational process design and optimization. What is required is a mathematical model which allows the effluent concentration to be predicted for any defined change in the feed concentration or flow rate to the bed. The flow pattern can generally be represented adequately by the axial dispersed plug-flow model, according to which a mass balance for an element of the column yields, for the basic differential equation governing llie dynamic behavior,... [Pg.37]

This is the simplest model of an electrocatalyst system where the single energy dissipation is caused by the ohmic drop of the electrolyte, with no influence of the charge transfer in the electrochemical reaction. Thus, fast electrochemical reactions occur at current densities that are far from the limiting current density. The partial differential equation governing the potential distribution in the solution can be derived from the Laplace Equation 13.5. This equation also governs the conduction of heat in solids, steady-state diffusion, and electrostatic fields. The electric potential immediately adjacent to the electrocatalyst is modeled as a constant potential surface, and the current density is proportional to its gradient ... [Pg.297]

Fig. < . Population evolution of eight coupled states in a CHjF (0.17 torr)-argon (10 torr) mixture. The time dependence of the population is calculated from a numerical integration of the differential equations governing the rate processes of equations 19a, 19b, 20, 21, 28. The magnitudes of the rate constants are taken from Refs. 19, 35, and 55. All populations are shown normalized to 10,000 for the peak of the population of a given state. The laser pulse occurs at t> 0. Only V-V processes are included in the model. Fig. < . Population evolution of eight coupled states in a CHjF (0.17 torr)-argon (10 torr) mixture. The time dependence of the population is calculated from a numerical integration of the differential equations governing the rate processes of equations 19a, 19b, 20, 21, 28. The magnitudes of the rate constants are taken from Refs. 19, 35, and 55. All populations are shown normalized to 10,000 for the peak of the population of a given state. The laser pulse occurs at t> 0. Only V-V processes are included in the model.
As with the simple models from Chapter 3, each different mechanical model can be described by a differential equation. The differential equation governing the response for any mechanical model may be obtained by considering the constitutive equations for each element as well as the overall equilibrium and kinematic constraints of the network. Once the differential equation is obtained, the response of the model to any desired loading can be examined by solving the differential equation for that particular loading. The solution for simple creep or relaxation loading will provide the creep compliance or the relaxation modulus for the given model. In this... [Pg.160]

The differential equation governing the relationship between stress and strain for a given mechanical model is quite valuable, but needs to be solved in order to determine the model response to specific loading conditions. Fundamental viscoelastic properties such as the creep compliance or relaxation modulus can be found by solution of the differential equation to the appropriate loading. For example, the creep compliance can be determined using the conditions for a creep test of constant stress, as shown in Fig. 5.2. [Pg.162]

Homogeneous liquid in a uniform linear core. The pressure partial differential equation governing transient, compressible, lineal, homogeneous, liquid flows having constant properties is 6 p(x,t)/9 = (( )pc/k) dpidi. Here p is pressure, while x and t represent space and time ( ), k, p, and e are rock porosity, rock permeability, fluid viscosity, and net fluid-rock compressibihty, respectively. If we assume a eonstant density, incompressible flow, and ignore the eompressibility of the fluid by setting c = 0, the right side of this equation identically vanishes. Then, the model reduces to the ordinary differential equation d p(x t)/d = 0 where t is a parameter as opposed to a variable. [Pg.307]

The chaotic nature of individual MD trajectories has been well appreciated. A small change in initial conditions (e.g., a fraction of an Angstrom difference in Cartesian coordinates) can lead to exponentially-diverging trajectories in a relatively short time. The larger the initial difference and/or the timestep, the more rapid this Lyapunov instability. Fig. 1 reports observed behavior for the dynamics of a butane molecule. The governing Newtonian model is the following set of two first-order differential equations ... [Pg.228]

This discussion suggests that even the reference trajectories used by symplectic integrators such as Verlet may not be sufficiently accurate in this more rigorous sense. They are quite reasonable, however, if one requires, for example, that trajectories capture the spectral densities associated with the fastest motions in accord to the governing model [13, 15]. Furthermore, other approaches, including nonsymplectic integrators and trajectories based on stochastic differential equations, can also be suitable in this case when carefully formulated. [Pg.232]

Differential-Algebraic Systems Sometimes models involve ordinary differentia equations subject to some algebraic constraints. For example, the equations governing one equihbrium stage (as in a distillation column) are... [Pg.474]

Transient Heat Conduction. Our next simulation might be used to model the transient temperature history in a slab of material placed suddenly in a heated press, as is frequently done in lamination processing. This is a classical problem with a well known closed solution it is governed by the much-studied differential equation (3T/3x) - q(3 T/3x ), where here a - (k/pc) is the thermal diffuslvity. This analysis is also identical to transient species diffusion or flow near a suddenly accelerated flat plate, if q is suitably interpreted (6). [Pg.274]

In the first chapter several traditional types of physical models were discussed. These models rely on the physical concepts of energies and forces to guide the actions of molecules or other species, and are customarily expressed mathematically in terms of coupled sets of ordinary or partial differential equations. Most traditional models are deterministic in nature— that is, the results of simulations based on these models are completely determined by the force fields employed and the initial conditions of the simulations. In this chapter a very different approach is introduced, one in which the behaviors of the species under investigation are governed not by forces and energies, but by rules. The rules, as we shall see, can be either deterministic or probabilistic, the latter leading to important new insights and possibilities. This new approach relies on the use of cellular automata. [Pg.9]

The modeling of steady-state problems in combustion and heat and mass transfer can often be reduced to the solution of a system of ordinary or partial differential equations. In many of these systems the governing equations are highly nonlinear and one must employ numerical methods to obtain approximate solutions. The solutions of these problems can also depend upon one or more physical/chemical parameters. For example, the parameters may include the strain rate or the equivalence ratio in a counterflow premixed laminar flame (1-2). In some cases the combustion scientist is interested in knowing how the system mil behave if one or more of these parameters is varied. This information can be obtained by applying a first-order sensitivity analysis to the physical system (3). In other cases, the researcher may want to know how the system actually behaves as the parameters are adjusted. As an example, in the counterflow premixed laminar flame problem, a solution could be obtained for a specified value of the strain... [Pg.404]

Let us first concentrate on dynamic systems described by a set of ordinary differential equations (ODEs). In certain occasions the governing ordinary differential equations can be solved analytically and as far as parameter estimation is concerned, the problem is described by a set of algebraic equations. If however, the ODEs cannot be solved analytically, the mathematical model is more complex. In general, the model equations can be written in the form... [Pg.11]

In some cases besides the governing algebraic or differential equations, the mathematical model that describes the physical system under investigation is accompanied with a set of constraints. These are either equality or inequality constraints that must be satisfied when the parameters converge to their best values. The constraints may be simply on the parameter values, e.g., a reaction rate constant must be positive, or on the response variables. The latter are often encountered in thermodynamic problems where the parameters should be such that the calculated thermophysical properties satisfy all constraints imposed by thermodynamic laws. We shall first consider equality constraints and subsequently inequality constraints. [Pg.158]

Given the governing differential equations (the model) and the initial conditions, xo> determine the optimal inputs, u(t), so that the determinant (for the volume criterion) or the smallest eigenvalue (for the shape criterion) of matrix Ane v (given by Equation 12.18) is maximized... [Pg.201]

The outline of this paper is as follows. First, a theoretical model of unsteady motions in a combustion chamber with feedback control is constructed. The formulation is based on a generalized wave equation which accommodates all influences of acoustic wave motions and combustion responses. Control actions are achieved by injecting secondary fuel into the chamber, with its instantaneous mass flow rate determined by a robust controller. Physically, the reaction of the injected fuel with the primary combustion flow produces a modulated distribution of external forcing to the oscillatory flowfield, and it can be modeled conveniently by an assembly of point actuators. After a procedure equivalent to the Galerkin method, the governing wave equation reduces to a system of ordinary differential equations with time-delayed inputs for the amplitude of each acoustic mode, serving as the basis for the controller design. [Pg.357]

With a few exceptions one can say that a flowing polymer melt does not follow the model presented in eqn. (5.20). To properly model the flow of a polymer we must take into account the effects of rate of deformation, temperature and often time, making the partial differential equations that govern a system non-linear. [Pg.217]


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Differential Equation Models

Differential models

Governing equations

Model equations

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Modelling equations

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