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Model solutions analytical solution

There also exists an alternative theoretical approach to the problem of interest which goes back to "precomputer epoch" and consists in the elaboration of simple models permitting analytical solutions based on prevailing factors only. Among weaknesses of such approaches is an a priori impossibility of quantitative-precise reproduction for the characteristics measured. Unlike articles on computer simulation in which vast tables of calculated data are provided and computational tools (most often restricted to standard computational methods) are only mentioned, the articles devoted to analytical models abound with mathematical details seemingly of no value for experimentalists and present few, if any, quantitative results that could be correlated to experimentally obtained data. It is apparently for this reason that interest in theoretical approaches of this kind has waned in recent years. [Pg.2]

Table XV. Anthocyanin and Tannin Coloration of Model Solutions, Analytical Results... Table XV. Anthocyanin and Tannin Coloration of Model Solutions, Analytical Results...
Using the dusty gas model [5] analytical solutions are derived to describe the internal pressure gradients and the dependence of the effective diffusion coefficient on the gas composition. Use of the binary flow model (BFM, Chapter 3) would also have yielded almost similar results to those discussed below. After discussion of the dusty gas model, results are then implemented in the Aris numbers. Finally, negligibility criteria are derived, this time for intraparticle pressure gradients. Calculations are given in appendices here we focus on the results. [Pg.159]

This model is of interest because it can be easily reduced to a hyperbolic form of the transport model of one property. With some particular univocity conditions, this hyperbolic model accepts analytical solutions, which are similar to those of an equivalent parabolic model. The hyperbolic model for the transport of a property is obtained by coupling the equation P(x, t) = Pj(x, t) + P2(x, t) to relations (4.267) and then eliminating the terms Pj(x, t) and Pj(x, t). The result can be written as ... [Pg.289]

It should be noted that if the open-loop response is evaluated by numerical integration, there is no requirement for linearity of the process model. Convenient analytical solutions can be found for some linear systems, such as series stirred tanks with instantaneous reaction and constant flow. [Pg.327]

In addition, an exact algebraic solution for the incubation period of bottom-up filling has been described for the situation when catalyst is pre-adsorbed and negligible consumption occurs during subsequent metal deposition [344], As with the string model, this analytical solution captures the essential aspects of the shape transitions that accompany the trench superfilling CEAC dynamic. The analytical solution also provides a metric for evaluating the accuracy of numerical models and associated computer codes. [Pg.165]

In Chapter 14, we discussed the case of a single-component band. In practice, there are almost always several components present simultaneously, and they have different mass transfer properties. As seen in Chapter 4, the equilibrium isotherms of the different components of a mixture depend on the concentrations of all the components. Thus, as seen in Chapters 11 to 13, the mass balances of the different components are coupled, which makes more complex the solution of the multicomponent kinetic models. Because of the complexity of these models, approximate analytical solutions can be obtained only under the assumption of constant pattern conditions. In all other cases, only numerical solutions are possible. The problem is further complicated because the diffusion coefficients and the rate constants depend on the concentrations of the corresponding components and of all the other feed components. However, there are still relatively few papers that discuss this second form of coupling between component band profiles in great detail. In most cases, the investigations of mass transfer kinetics and the use of the kinetic models of chromatography in the literature assume that the rate constants and the diffusion coefficients are concentration independent. This seems to be an acceptable first-order approximation in many cases, albeit separation problems in which more sophisticated theoretical approaches are needed begin to appear as the accuracy of measru ments improve and more interest is paid to complex... [Pg.735]

For a single-zone equivalent TMB model, an analytical solution is available for a linear isotherm, considering both axial mixing and a finite rate of mass transfer which is accounted for with the linear driving force (LDF) model model 2a) [18]. [Pg.785]

Neither the Hubbard model nor the Heisenberg model have analytic solutions even for the ground state in higher than one dimension... [Pg.132]

In theoretical studies, one usually deals with two simple models for the solvent relaxation, namely, the Debye model with the Lorentzian form of the frequency dependence, and the Ohmic model with an exponential cut-off [71, 85, 188, 203]. The Debye model can work well at low frequencies (long times) but it predicts nonanalytic behavior of the time correlation function at time zero. Exponential cut-off function takes care of this problem. Generalized sub- and super-Ohmic models are sometimes considered, characterized by a power dependence on CO (the dependence is linear for the usual Ohmic model) and the same exponential cut-off [203]. All these models admit analytical solutions for the ET rate in the Golden Rule limit [46,48]. One sometimes includes discrete modes or shifted Debye modes to mimic certain properties of the real spectrum [188]. In going beyond the Golden Rule limit, simplified models are considered, such as a frequency-independent (strict Ohmic) bath [71, 85, 203], or a sluggish (adiabatic)... [Pg.523]

Due to the complexity of most of these models, an analytical solution is intractable. Therefore, one often relies on numerical integration (for low dimensions) or MCMC methods such as the Metropolis-Hastings (Hastings, 1970 Metropolis et al., 1953) or Gibbs sampler algorithms (Gelfand and Smith, 1990). [Pg.271]

Ouyang, Z. and Li, G. (2009) Cohesive zone model based analytical solutions for adhesively bonded pipe joints under torsional loading. International Journal of Solids and Structures, 46, 1205-1217. [Pg.353]

The performances of the 3D CZM model were compared with a previously developed 2D model and analytical solutions on mode I, mode II and mixed-mode I/n loaded cracks in bonded aluminum or composite assemblies. The results are in an overall good agreement with each other, with the exception of the first instants of propagation of the 3D model, where the CZM process zone has to shape up. Next step should to assess this initial transient of 3D process zone formation, leading to a higher predicted number of cycles with respect to 2D simulation, by experimental evidence. [Pg.142]

For a given electrolyte composition and solvent reduction product, c, Cp, and A are all determined and thus are not adjustable parameters. Only the solvent diffusivity in the SEI may serve as an adjustable empirical parameter in this model. Finally, the model s analytical solution yields... [Pg.294]

Consider the analytical versus the numerical solution. Analytical solutions are only possible for special situations essentially die problem has to be linear. Most often, a numerical solution is the only option luckily the cost of computers is low and models can run in parallel on computer clusters if necessary. [Pg.7]

Debye s model gives only an approximate deseription of the vibrational properties of real solids, espeeially for solids eontaining different atoms or having certain lattice structures. However, it is very convenient in situations where an analytical expression for the distribution functions is necessary, because more rigorous models give analytical solutions for one- or two-dimensional systems only. Since the spectra of surface vibrations are much more complicated, this model is often used. There are also some empirical combinations of Debye and Einstein distributions (in the classical limit) ... [Pg.420]

Cummings P T and Stell G 1984 Statistical mechanical models of chemical reactions analytic solution of models of A + S AS in the Percus-Yevick approximation Mol. Phys. 51 253... [Pg.554]

This solution can be obtained explicitly either by matrix diagonalization or by other techniques (see chapter A3.4 and [42, 43]). In many cases the discrete quantum level labels in equation (A3.13.24) can be replaced by a continuous energy variable and the populations by a population density p(E), with replacement of the sum by appropriate integrals [Hj. This approach can be made the starting point of usefiil analytical solutions for certain simple model systems [H, 19, 44, 45 and 46]. [Pg.1051]

This can be solved analytically only for a few simplified systems. The Onsager model uses one of the known analytic solutions. [Pg.209]

In this section we proceed to study the plate model with the crack described in Sections 2.4, 2.5. The corresponding variational inequality is analysed provided that the nonpenetration condition holds. By the principles of Section 1.3, we propose approximate equations in the two-dimensional case and analytical solutions in the one-dimensional case (see Kovtunenko, 1996b, 1997b). [Pg.118]

In this section we deal with the simplified nonpenetration condition of the crack faces considered in the previous section. We formulate the model of a plate with a crack accounting for only horizontal displacements and construct approximate equations using penalty and iterative methods. The convergence of these solutions is proved and its application to the onedimensional problem is discussed. Analytical solutions for the model of a bar with a cut are obtained. The results of this section can be found in (Kovtunenko, 1996c, 1996d). [Pg.159]

UNIFAC andASOG Development. Pertinent equations of the UNIQUAC functional-group activity coefficient (UNIFAC) model for prediction of activity coefficients including example calculations are available (162). Much of the background of UNIFAC involves another QSAR technique, the analytical solution of groups (ASOG) method (163). [Pg.249]

Simulation of Dynamic Models Linear dynamic models are particularly useful for analyzing control-system behavior. The insight gained through linear analysis is invaluable. However, accurate dynamic process models can involve large sets of nonlinear equations. Analytical solution of these models is not possible. Thus, in these cases, one must turn to simulation approaches to study process dynamics and the effect of process control. Equation (8-3) will be used to illustrate the simulation of nonhnear processes. If dcjdi on the left-hand side of Eq. (8-3) is replaced with its finite difference approximation, one gets ... [Pg.720]

In general, fiiU time-dependent analytical solutions to differential equation-based models of the above mechanisms have not been found for nonhnear isotherms. Only for reaction kinetics with the constant separation faclor isotherm has a full solution been found [Thomas, y. Amei Chem. Soc., 66, 1664 (1944)]. Referred to as the Thomas solution, it has been extensively studied [Amundson, J. Phy.s. Colloid Chem., 54, 812 (1950) Hiester and Vermeiilen, Chem. Eng. Progre.s.s, 48, 505 (1952) Gilliland and Baddonr, Jnd. Eng. Chem., 45, 330 (1953) Vermenlen, Adv. in Chem. Eng., 2, 147 (1958)]. The solution to Eqs. (16-130) and (16-130) for the same boimdaiy condifions as Eq. (16-146) is... [Pg.1529]

Analytical solutions also are possible when T is constant and m = 0, V2, or 2. More complex chemical rate equations will require numerical solutions. Such rate equations are apphed to the sizing of plug flow, CSTR, and dispersion reactor models by Ramachandran and Chaud-hari (Three-Pha.se Chemical Reactors, Gordon and Breach, 1983). [Pg.2119]

If the puncture occurs on a pipe which is at least 0.5 m from a vessel, it is justifiable to use a homogeneou.s equilibrium model (HEM) for which an analytical solution is available. The discharge rate pre-... [Pg.2346]

The parameters for the model were originally evaluated for oil shale, a material for which substantial fracture stress and fragment size data depending on strain rate were available (see Fig. 8.11). In the case of a less well-characterized brittle material, the parameters may be inferred from the shear-wave velocity and a dynamic fracture or spall stress at a known strain rate. In particular, is approximately one-third the shear-wave velocity, m has been shown to be about 6 for various brittle materials (Grady and Lipkin, 1980), and k can then be determined from a known dynamic fracture stress using an analytic solution of (8.65), (8.66) and (8.68) in one dimension for constant strain rate. [Pg.315]


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