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The Continuous Model

In the continuous model we take v to be the velocity of the fluid and define a matrix K of thermal conductivities. This matrix has elements Ky and the rate of transfer of heat in the ith direction (i = 1,2) is [Pg.342]


This section is divided into three parts. The first is a comparison between the experimental data reported by Wisseroth (].)for semibatch polymerization and the calculations of the kinetic model GASPP. The comparisons are largely graphical, with data shown as point symbols and model calculations as solid curves. The second part is a comparison between some semibatch reactor results and the calculations of the continuous model C0NGAS. Finally, the third part discusses the effects of certain important process variables on catalyst yields and production rates, based on the models. [Pg.207]

Figure 5 is a plot of the calculated polymer yields from the continuous model C0NGAS vs. the yields from the semibatch model... [Pg.211]

Fig. 10.3 Ideas concerning crystals /e/ the continuous model of Hairy with cubic particles, right ihe nowadays model of ionic lattice... Fig. 10.3 Ideas concerning crystals /e/ the continuous model of Hairy with cubic particles, right ihe nowadays model of ionic lattice...
Figure 2.6. Energy level diagram (top) and spectra (bottom) illustrating the continuous model of relaxation. The energy of the emitted quanta decreases (hvF- kv F- hvF) and the position of the fluorescence spectrum (solid curves) moves smoothly as a result of relaxation. Figure 2.6. Energy level diagram (top) and spectra (bottom) illustrating the continuous model of relaxation. The energy of the emitted quanta decreases (hvF- kv F- hvF) and the position of the fluorescence spectrum (solid curves) moves smoothly as a result of relaxation.
Microscopically, the interface reaction during crystal growth may be through various mechanisms. One mechanism is called the continuous model. Two other models are layer-spreading models. [Pg.348]

This is the first of several chapters which deal with the construction of models of environmental systems. Rather than focusing on the physical and chemical processes themselves, we will show how these processes can be combined. The importance of modeling has been repeatedly mentioned before, for instance, in Chapter 1 and in the introduction to Part IV. The rationale of modeling in environmental sciences will be discussed in more detail in Section 21.1. Section 21.2 deals with both linear and nonlinear one-box models. They will be further developed into two-box models in Section 21.3. A systematic discussion of the properties and the behavior of linear multibox models will be given in Section 21.4. This section leads to Chapter 22, in which variation in space is described by continuous functions rather than by a series of homogeneous boxes. In a sense the continuous models can be envisioned as box models with an infinite number of boxes. [Pg.947]

To compare computer simulations with an analytical theory, it is convenient to introduce a distinctive parameter - dimensionless saturation concentration Uq = n(co)vo, where n(oo) is stationary concentration of accumulated defects at their saturation (t —> oo). (It is assumed that n(t) = n (t) = n t), vo is volume of the d-dimensional sphere having the recombination radius r0 v0 = 7iro/d.) In the continuous model it is clear that the quantity Uo, if it exists, is a universal parameter dependent on d only but not on vq. Indeed, most of previous theoretical studies were aimed mainly to obtain Uo-... [Pg.389]

Rigorous formulations of the problems associated with solvation necessitate approximations. From the computational point of view, we are forced to consider interactions between a solute and a large number of solvent molecules which requires approximate models [75]. The microscopic representation of solvent constitutes a discrete model consisting of the solute surrounded by individual solvent molecules, generally only those in close proximity. The continuous model considers all the molecules surrounding the solvent but not in a discrete representation. The solvent is represented by a polarizable dielectric continuous medium characterized by macroscopic properties. These approximations, and the use of potentials, which must be estimated with empirical or approximate computational techniques, allows for calculations of the interaction energy [75],... [Pg.229]

The stochastic models can present discrete or continuous forms. The former discussion was centred on discrete models. The continuous models are developed according to the same base as the discrete ones. Example 4.3.1 has already shown this method, which leads to a continuous stochastic model. This case can be gen-... [Pg.220]

Consider the numerical inversion of Eq. (1), that is, the calculation of w%V) from the knowledge of w V) and g(V, To)- To this effect, let us first transform the continuous model of Eq. (1) into the following equivalent discrete model ... [Pg.204]

This approach, the stage model, is simple because the equations are first-order ordinary differential ones that can be easily solved by Gear s algorithm. However, it is less accurate than the continuous model, especially when dealing with columns... [Pg.844]

It is well known that the energy of interaction of an atom with the continuous solid is 2-3 times less than with the discrete (atomic) model (cf., e.g., Ref. [38], Figs. 2.2-2.4). Thus, to obtain the same Henry s Law constants with the two models, one has to increase e for the continuous model. This, however, does not discredit the continuous model which is frequently used in adsorption calculations. In particular, we can use the above mentioned results of Ref. [37] to predict the value of e for Ar which would have been obtained if one had carried out Henry s Law constant calculations for Ar in the AO model of Ref. [17] and compared them with experiment. One can multiply the value of e for CH4 obtained from AO model by the ratio of e values for Ar and CH4 in the CM model [36] to obtain tjk = 165A for Ar in the AO model. This is very close to the value of 160 K obtained in Ref. [21, 28] by an independent method in which the value of the LJ parameter e for the Ar - oxide ion interaction was chosen to match the results of computer simulation of the adsorption isotherm on the nonporous heterogeneons surface of Ti02. Considering the independence of the calculations and the different character of the adsorbents (porous and nonporous), the closeness of the values of is remarkable (if it is not accidental). The result seems even more remarkable in the light of discussion presented in Ref. [28]. Another line of research has dealt with the influence of porous structure of the silica gel upon the temperature dependence of the Henry constants [36]. [Pg.348]

In conclusion, although the continuous models have some distinct advantages, the literature survey indicates that the most popular are still the discrete models, which offer various types of approaches that enable the explanation of complexation of metal ions by HSs. [Pg.131]

Within the approach developed in the previous section, neither of these assumptions can be replaced easily by a more realistic one. However, it turns out that, if one abandons the continuous model fluid in favor of a discrete model in whicli molecules are restricted to positions on a rigid lattice, the second of the above assumptions is no longer necessary to derive an analytic expression for the partition function of the fluid. [Pg.115]

Because of the similarity between the lattice fluid calculations and the MC simulations for the continuous model, it seems instructive to study the phase behavior in the latter if the confined fluid is exposed to a shear strain. This may be done quantitatively by calculating p as a function of p and as -For sufficiently low p, one expects a gas-like phase to exist along a subcritical isotherm (see Fig. 4.13) defined as the set of points (T = const)... [Pg.256]

The assumption of homogeneity can be abandoned if the continuous me m-field treatment is replaced by a discrete treatment where the positions of fluid molecules are restricted to nodes on a lattice. The discussion in Section 5.4.2 and 5.6.5 showed that the mean-field lattice density functional theory developed in Section 4.3 w as crucial in unraveling the c.om-plex phase behavior of fluids confined by chemically decorated substrate surfaces. A similar deep understanding of the phase behavior would not have been possible on the basis of simulation results alone. Nevertheless, the relation between these MC data and the lattice density functional results remained only qualitative on accoimt of the continuous models employed in the computer simulations. Thus, we aim at a more quantitative comparison between MC simulations and mean-field lattice density fimctioiial theory in the closing. section of this diaptcr. [Pg.292]

The lattice models or the models with discrete links in continuous space do not enable the theoretician to pursue theoretical calculations very far. At best, they can be used if the theoretician is content with the tree approximation which will be studied later on. On the contrary, the continuous models are more adapted to analytical calculations. As a counterpart, divergences appear, but, as will be... [Pg.354]

ANOTHER FORMULATION OF THE CONTINUOUS MODEL EDWARDS S TRANSFORMATION... [Pg.358]

The contributions of the general diagrams can be expressed in terms of those of the connected diagrams, and precise relations between these contributions will be given here in order to justify the results announced in the preceding section. For this purpose, it is convenient to use a very general simplified notation. Indeed, the results are not only true for the continuous model but also for the discrete-link model in continuous space (Ursell-Mayer-Yvon expansions) and for lattice models. [Pg.380]

Entropy can also be calculated by starting from the continuous model and, in this case, we expect a similar result. However, we must note that in the continuous case, the entropy of the system is really infinite and that a finite entropy can be obtained only after performing a subtractive renormalization. Actually, this question has been tackled several times, either indirectly with the help of a zero component field theory,3,4 or by using the direct renormalization method.2 We shall now describe in detail the latter approach. [Pg.544]


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Continuous chain limit and the Edwards model

Continuous model

Existence of the equivalent continuous chain model

Fields associated with the standard continuous model

Kinetic Models in the Form of Equations Containing Piecewise Continuous Functions

Model 2 The Ideal Continuous Stirred Tank Reactor (CSTR) with V Constant

Predictive Modeling of the Continuous Catalyst Regeneration (CCR) Reforming Process

Renormalizability of the continuous chain model

The Continuous Rouse Model

The continuous inverse model

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