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Dynamic behavior of ideal systems

Finally, "data" can be obtained from computer simulations (26), whether deterministic (molecular dynamics) or stochastic (Monte Carlo). This approach provides a level of microscopic detail not available with any of the above experimental techniques. Results from computer simulations, furthermore, can be both qualitative (for example, observation of cavity dynamics in repulsive supercritical systems (12)) as well as quantitative. However, because true intermolecular potentials are not known exactly, simulation results must be interpreted with caution, especially if they are used to study the behavior of real systems. Through simulations, therefore, one obtains exact answers to ideal (as opposed to real) problems. [Pg.65]

The two extreme hypotheses on mixing produce lumped models for the fluid dynamic behavior, whereas real reactors show complex mixing patterns and thus gradients of composition and temperature. It is worthwhile to stress that the fluid dynamic behavior of real reactors strongly depends on their physical dimensions. Moreover, in ideal reactors the chemical reactions are supposed to occur in a single phase (gaseous or liquid), whereas real reactors are often multiphase systems. Two simple examples are the gas-liquid reactors, used to oxidize a reactant dissolved in a liquid solvent and the fermenters, where reactions take place within a solid biomass dispersed in a liquid phase. Real batch reactors are briefly discussed in Chap. 7, in the context of suggestions for future research work. [Pg.11]

First, and most important, nonlinear dynamics provides an intellectual framework to pursue the consequences of nonlinear behavior of transport systems, which is simply not possible in an intellectual environment that is based upon a linear mentality, characterized by well-behaved, regular solutions of idealized problems. One example that illustrates the point is the phenomenon of hydrodynamic dispersion in creeping flows of nondilute suspensions. It is well known that Stokes flows are exactly reversible in the sense that the particle trajectories are precisely retraced when the direction of the mean flow is reversed. Nevertheless, the lack of reversibility that characterizes hydrodynamic dispersion in such suspensions has been recently measured experimentally [17] and simulated numerically [18], Although this was initially attributed to the influence of nonhydrodynamic interactions among the particles [17], the numerical simulation [18] specifically excludes such effects. A more general view is that the dispersion observed is a consequence of (1) deterministic chaos that causes infinitesimal uncertainties in particle position (due to arbitrarily weak disturbances of any kind—... [Pg.68]

Fig. 10.8. Different types of image distortions. The small circles mark the reference positions in an ideal 2-D grid, the crosses indicate the measured positions. Depending on their origin, these errors are either temporary, permanent or of dynamic nature. Hence, the dynamic behavior of the scan system has to be taken into account when performing a lateral calibration. The scan speed may even have a greater influence on the actual correction factor than the scan range. Further to be considered are the digital resolution (in z-direction) and the number of pixels (in x-y-direction). Fig. 10.8. Different types of image distortions. The small circles mark the reference positions in an ideal 2-D grid, the crosses indicate the measured positions. Depending on their origin, these errors are either temporary, permanent or of dynamic nature. Hence, the dynamic behavior of the scan system has to be taken into account when performing a lateral calibration. The scan speed may even have a greater influence on the actual correction factor than the scan range. Further to be considered are the digital resolution (in z-direction) and the number of pixels (in x-y-direction).
As known, SEC separates molecules and particles according to their hydro-dynamic volume in solution. In an ideal case, the SEC separation is based solely on entropy changes and is not accompanied with any enthalpic processes. In real systems, however, enthalpic interactions among components of the chromatographic system often play a nonnegligible role and affect the corresponding retention volumes (Vr) of samples. This is clearly evident from the elution behavior of small molecules, which depends rather strongly on their chemical nature and on the properties of eluent used. This is the case even for... [Pg.445]

The preceding discussion was limited mostly to VP processes occurring by direct coupling of the quasibound state of the complex to the dissociative continuum, which is the simplest and most commonly observed decay route for the complexes. However, these systems also serve as ideal venues for studying an array of more complicated dynamical processes, including IVR, and electronic predissociation. This brief section will focus on the former, underscoring some of the inherent dynamical differences between Rg XY complexes by discussing the IVR behavior of a few systems. [Pg.410]

Different types of liquid crystals exhibit different rheological properties [16,17]. With an increase in organization of the microstructure of the liquid crystal its consistency increases and the flow behavior becomes more viscous. The coefficient of dynamic viscosity r, although a criterion for the viscosity of ideal viscous flow behavior (Newtonian systems), is high for cubic and hexagonal liquid crystals but fairly low for lamellar ones. However, the flow characteristics are not Newtonian but plastic or pseudoplastic, respectively. [Pg.132]

Pressure-dependent sorption and transport properties in polymers can be attributed to the presence of the penetrant in the polymer. Crank (32) suggested in 1953 that the "non-ideal" behavior of penetrant-polymer systems could arise from structural and dynamic changes of the polymer in response to the penetrant. As the properties of the polymer are dependent on the nature and concentration of the penetrant, the solubility and diffusion coefficient are also concentration-dependent. The concentration-dependent sorption and transport model suggests that "non-ideal" penetrant-polymer systems still obey Henry s and Fick s laws, and differ from the "ideal" systems only by the fact that a and D are concentration dependent,... [Pg.104]

To examine the behavior of mixing measures, it is useful to begin by considering systems free of experimental uncertainties. Particle dynamic simulations such as those discussed in the sections Mixing mechanism in Three Dimensional Tumblers and Demixing, represent such ideal systems the presence and locations of all particles are known and are free of sampling errors (discussed in the section on Sampling Techniques ). [Pg.2361]

Dynamic analysis of this ideal ABC, 2photochemical reaction A - B, < >AB is balanced by the fast thermal back-relation B —> A, fcBA B does not accumulate, the photochemical reaction B - C, <()BC does not take place, and the system stabilizes into a steady state enriched in A ([C] 0). On the other hand, if Iq is high, B forms and C is then produced C is relatively stable as the thermal reaction cA is slow, and the system stabilizes into a steady state enriched in C. [Pg.190]

Dynamic analysis is also a powerful method for the study of complex behavior. The description of an ideal ABC system with the possibility of multiple photostationary states illustrates the dynamic bistable behavior of TPID. [Pg.194]

The elution profile of an ideal chromatogram depends only on the thermodynamic behavior of the chromatographic system. In a real chromatogram additional mass transfer and fluid dynamic factors have to be taken into account. [Pg.18]


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See also in sourсe #XX -- [ Pg.400 , Pg.410 ]

See also in sourсe #XX -- [ Pg.400 , Pg.401 , Pg.402 , Pg.403 , Pg.404 , Pg.405 , Pg.406 , Pg.407 , Pg.408 , Pg.409 ]




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