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Spatial uniformity

The classical experiment tracks the off-gas composition as a function of temperature at fixed residence time and oxidant level. Treating feed disappearance as first order, the pre-exponential factor and activation energy, E, in the Arrhenius expression (eq. 35) can be obtained. These studies tend to confirm large activation energies typical of the bond mpture mechanism assumed earlier. However, an accelerating effect of the oxidant is also evident in some results, so that the thermal mpture mechanism probably overestimates the time requirement by as much as several orders of magnitude (39). Measurements at several levels of oxidant concentration are useful for determining how important it is to maintain spatial uniformity of oxidant concentration in the incinerator. [Pg.57]

Cathodoluminescence microscopy and spectroscopy techniques are powerful tools for analyzing the spatial uniformity of stresses in mismatched heterostructures, such as GaAs/Si and GaAs/InP. The stresses in such systems are due to the difference in thermal expansion coefficients between the epitaxial layer and the substrate. The presence of stress in the epitaxial layer leads to the modification of the band structure, and thus affects its electronic properties it also can cause the migration of dislocations, which may lead to the degradation of optoelectronic devices based on such mismatched heterostructures. This application employs low-temperature (preferably liquid-helium) CL microscopy and spectroscopy in conjunction with the known behavior of the optical transitions in the presence of stress to analyze the spatial uniformity of stress in GaAs epitaxial layers. This analysis can reveal,... [Pg.156]

Figure 5.18. Schematic representation of the density of states N(E) in the conduction band and of the definitions of work function d>, chemical potential of electrons p, electrochemical potential of electrons or Fermi level p, surface potential x> Galvani (or inner) potential

Figure 5.18. Schematic representation of the density of states N(E) in the conduction band and of the definitions of work function d>, chemical potential of electrons p, electrochemical potential of electrons or Fermi level p, surface potential x> Galvani (or inner) potential <p and Volta (or outer) potential T for the catalyst (W) and for the reference electrode (R). The measured potential difference Uwr is by definition the difference in Fermi levels <p, p and p are spatially uniform O and can vary locally on the metal sample surfaces and the T potentials vanish, on the average, for the (effective double layer covered) gas-exposed catalyst and reference electrode surfaces.32 Reprinted with permission from The Electrochemical Society.
The difficulty disappears when the mixing and mass transfer steps are fast compared with the reaction steps. The contents of the reactor remain perfectly mixed even while new ingredients are being added. Compositions and reaction rates will be spatially uniform, and a flow term is simply added to the mass balance. Instead of Equation (2.30), we write... [Pg.65]

In the presence of a static, spatially uniform electric field Ea, the electronic cloud of atomic and molecular systems gets polarized. The energy, W, can be written as a Taylor series [1-3]... [Pg.279]

A stream leaving a well-mixed region, such as a well-stirred tank, has the identical properties as in the system, since for perfect mixing the contents of the tank will have spatially uniform properties, which must then be identical to the properties of the fluid leaving at the outlet. Thus, the concentrations of component i both within the tank and in the tank effluent are the same and equal to Cj], as shown in Fig. 1.11. [Pg.24]

First, it is assumed that the EEDF is spatially uniform and temporally constant, which is allowed if the energy relaxation time of the EEDF is much shorter than the RF-cycle duration, and if the relaxation length is much smaller than the typical gradient scale length. This assumption implies a spatially and temporally constant electric field. It reduces the Boltzmann equation to a problem exclusively in the velocity space. [Pg.48]

Stirred tank models have been widely used in pharmaceutical research. They form the basis of the compartmental models of traditional and physiological pharmacokinetics and have also been used to describe drug bioconversion in the liver [1,2], drug absorption from the gastrointestinal tract [3], and the production of recombinant proteins in continuous flow fermenters [4], In this book, a more detailed development of stirred tank models can be found in Chapter 3, in which pharmacokinetic models are discussed by Dr. James Gallo. The conceptual and mathematical simplicity of stirred tank models ensures their continued use in pharmacokinetics and in other systems of pharmaceutical interest in which spatially uniform concentrations exist or can be assumed. [Pg.25]

Equation (64) provides just one example of a phenomenon that may easily occur whenever species with different migration characteristics equilibrate sluggishly with each other and especially when they obey different boundary conditions. Namely, in uniform material subjected to time-independent boundary conditions, a steady state can be approached at long times that is not spatially uniform. We shall note a possible manifestation of such an effect in Section 5 of III. [Pg.269]

More generally, deviations from spatial uniformity are expressed by non-vanishing Fourier indices moreover, all physical quantities of interest are directly expressed with the help of Fourier coefficients involving only a few non-vanishing wave numbers. [Pg.170]

We can find a spatially uniform solution for the quark wave function, ifw =... [Pg.255]

The solution of Eq. (6.137) must be combined with the nonsteady equations for the diffusion of heat and mass. This system can only be solved numerically and the computing time is substantial. Therefore, a simpler alternative model of droplet heating is adopted [26, 27], In this model, the droplet temperature is assumed to be spatially uniform at Ts and temporally varying. With this assumption Eq. (6.136) becomes... [Pg.362]

Since the solid—solid interface and bulk of the mixed conductor remain in chemical and electrical equilibrium, the measured overpotential t] is related directly to the spatially uniform oxidation state of the film through the Nemst equation 4Ft] = RTf d — (3o). Solving for d( and recognizing that the impedance Z = rjU, one obtains... [Pg.569]

In the remainder of this section, we give a brief overview of some of the functionals that are most widely used in plane-wave DFT calculations by examining each of the different approaches identified in Fig. 10.2 in turn. The simplest approximation to the true Kohn-Sham functional is the local density approximation (LDA). In the LDA, the local exchange-correlation potential in the Kohn-Sham equations [Eq. (1.5)] is defined as the exchange potential for the spatially uniform electron gas with the same density as the local electron density ... [Pg.216]

A batch reactor is defined as a closed spatially uniform system which has concentration parameters that are specified at time zero. It might look as illustrated in Figure 2-4. This requires that the system either be stirred rapidly (the propeller in Fig. 24) or started out spatially uniform so that stirring is not necessary. Composition and temperature are therefore independent of position in the reactor, so that the number of moles of species in the system Nj is a function of time alone. Since the system is closed (no flow in or out), we can write simply that the change in the total number of moles of species j in the reactor is equal to the stoichiometric coefficient Vj multiplied by the rate multiphed by the volume of the reactor. [Pg.38]

The PFTR was in fact assumed to be in a steady state in which no parameters vary with time (but they obviously vary with position), whereas the batch reactor is assumed to be spatially uniform and vary only with time. In the argument we switched to a moving coordinate system in which we traveled down the reactor with the fluid velocity , and in that case we follow the change in reactant molecules undergoing reaction as they move down the tube. This is identical to the situation in a batch reactor ... [Pg.96]


See other pages where Spatial uniformity is mentioned: [Pg.20]    [Pg.245]    [Pg.435]    [Pg.214]    [Pg.216]    [Pg.15]    [Pg.162]    [Pg.235]    [Pg.384]    [Pg.243]    [Pg.157]    [Pg.186]    [Pg.362]    [Pg.164]    [Pg.97]    [Pg.31]    [Pg.373]    [Pg.210]    [Pg.242]    [Pg.253]    [Pg.53]    [Pg.53]    [Pg.292]    [Pg.275]    [Pg.232]    [Pg.58]    [Pg.489]    [Pg.251]    [Pg.120]    [Pg.114]    [Pg.112]    [Pg.84]   
See also in sourсe #XX -- [ Pg.47 , Pg.89 ]




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