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Cylindrical geometry model

Boundary conditions are special treatments used for internal and external boundaries. For example, the center line in cylindrical geometry is an internal boundary that is modeled as a plane of symmetry. External boundaries model the world outside the mesh. The outermost row of elements is often used to implement the boundary condition as shown in Fig. 9.13. The mass, stress, velocity, etc., of the boundary elements are defined by the boundary conditions rather than the governing equations. External boundary conditions are typically prescribed through user input. [Pg.336]

For simplicity, the basic theoretical considerations of electrostatic precipitation are given in terms of cylindrical geometry, i.e., pipe-type electrostatic precipitation. This makes it possible to show most of the basic principles without numerical modeling. [Pg.1216]

By deriving or computing the Maxwell equation in the frame of a cylindrical geometry, it is possible to determine the modal structure for any refractive index shape. In this paragraph we are going to give a more intuitive model to determine the number of modes to be propagated. The refractive index profile allows to determine w and the numerical aperture NA = sin (3), as dehned in equation 2. The near held (hber output) and far field (diffracted beam) are related by a Fourier transform relationship Far field = TF(Near field). [Pg.291]

The analyses of simultaneous reaction and mass transfer in this geometry are similar mathematically to those of the straight cylindrical pore model considered previously, because both are essentally one-dimensional models. In the general case, the Thiele modulus for semiinfinite, flat-plate problems becomes... [Pg.451]

To simplify the treatment for an LFR in this chapter, we consider only isothermal, steady-state operation for cylindrical geometry, and for a simple system (A - products) at constant density. After considering uses of an LFR, we develop the material-balance (or continuity) equation for any kinetics, and then apply it to particular cases of power-law kinetics. Finally, we examine the results in relation to the segregated-flow model (SFM) developed in Chapter 13. [Pg.393]

Later, Paul and Paddison presented a statistical mechanical model that was used to calculate the dielectric permittivity in the water domains, that is, the pores, of Nafion.234 For computational purposes, a pore was taken as being of cylindrical geometry. The main prediction is that in a fully hydrated... [Pg.340]

A number of investigators have modeled the Tsuji and Yamaoka data [104]. In these investigations the flame was modeled as a semi-infinite stagnation flow, with the outer potential flow characterized by the velocity-gradient parameter a (see Section 6.3.1). For the cylindrical geometry, this characterization is correct in the neighborhood of the center stagnation-flow streamline. [Pg.703]

Kempter50 studied the thermal decomposition of 88% dense NbC cylinders from 2273 to 3473 K in 1 atm of He. Data at 3273 K will be used to test our diffusion-coupled vaporization mass loss model. We transposed the cylindrical geometry into an equivalent slab by dividing the volume by the average vaporizing area. One face of the cylinder was not included in the calculation because it rested on a NbC pedestal in the furnace. Table 3.13. summarizes analytical X-ray data for average C/Nb compositions. [Pg.51]

In the following, the equations defined in Chapter 3, and pertinent to the present model, are reported. Considering the single cell cylindrical geometry and the ribs... [Pg.99]

The formalism of nonlocal functional density theory provides an attractive way to describe the physical adsorption process at the fluid - solid interface.65 In particular, the ability to model adsorption in a pore of slit - like or cylindrical geometry has led to useful methods for extracting pore size distribution information from experimental adsorption isotherms. At the moment the model has only been tested for microporous carbons and slit - shaped materials.66,67 It is expected that the model will soon be implemented for silica surfaces. [Pg.55]

Within PB theory [2] and on the level of a cell model the cylindrical geometry can be treated exactly in the salt-free case [3, 4]. The Poisson-Boltzmann (PB) solution for the cell model is reviewed in the chapter in this volume on the osmotic coefficient. The PB approach can provide for instance new insights into the phenomenon of Manning condensation [5-7]. For example, the distance up to which counterions can be called condensed can be conveniently found via the inflection point in the log plot of the integrated radial distribution function P(r) of counterions [8, 9], defined as... [Pg.70]

The results obtained with the cylindrical pore geometry (Table 9.2) are in reasonable agreement with the reported experimental data [97], However, for the H-Y zeolite, the cylindrical pore model did not provide a good result, since the pore system of the zeolite Y resembles a three-dimensional cylindrical system [115], The appropriate model for the zeolite Y is the spherical geometry pore [107] in this regard, the results reported in Table 9.3 shows that only the zeolite Y is properly described with the spherical geometry pore model [97],... [Pg.440]

Figure 8.2 Cylindrical geometry of the Krogh-Erlang model of blood-tissue exchange. The upper panel, from Middleman [141], illustrates the assumed parallel arrangement of capillaries with each vessel independently supplying a surrounding cylinder of tissue. A diagram of the model geometry is provided in the lower panel. Figure in upper panel is reprinted with the permission of John Wiley Sons, Inc. Figure 8.2 Cylindrical geometry of the Krogh-Erlang model of blood-tissue exchange. The upper panel, from Middleman [141], illustrates the assumed parallel arrangement of capillaries with each vessel independently supplying a surrounding cylinder of tissue. A diagram of the model geometry is provided in the lower panel. Figure in upper panel is reprinted with the permission of John Wiley Sons, Inc.
In the numerical calculation of that experiment we use the axisymmetric version of the fluidized bed computer model to reproduce the cylindrical geometry of the reactor. The gas feed is simulated by a fully mixed stream of oxygen, steam and nitrogen which is injected at the base of the reactor within a radius of two-inches, corresponding to the radius through the centers of the injection cones in the actual six-cone feed gas distributor. [Pg.168]

Vycor is a porous silica glass which is widely used as a model structure for the. study of the properties of confined fluids in me.soporous materials. The pores in vycor have an average radius of about 30-35 A (assuming a cylindrical geometry) and are spaced about 200 A apart [2-3]. A literature survey indicates that there are two kinds of (Corning) vycor glasses one type has a specific surface around 100 m /g while the other is characterized by a specific surface around 200 m /g (both values are obtained from N2 adsorption isotherms at 77 K). [Pg.2]

The most commonly used model for pore topology is to represent the material as composed of independent, non-interconnected pores of some simple geometry usually these are of slit shape for activated carbons, and of cylindrical geometry for glasses, oxides, silicas, etc. Usually, the heterogeneity is approximated by a distribution of pore sizes, it being implicitly assumed that all pores are of the same geometry and surface chemistry. In this case the excess adsorption, f(P), at a pressure P can be represented by... [Pg.41]

The unreacted core model, suitably modified for cylindrical geometry, was used to describe the behavior... [Pg.1156]

In this section we present expressions for the mass transfer coefficients for diffusion in spherical and cylindrical geometries. The results presented here are useful in the modeling of mass transfer in, for example, gas bubbles in a liquid, liquid droplets in a gas, or gas jets in a liquid as shown in Figure 9.6. [Pg.235]

In these beds, pore size is determined by the number of nearest neighbors (coordination number) n, the sphere radius r, and the type of packing geometry. Two radii characterize the pore size one for the "throat" and one for the "cavity" of the pore (18). Isotherms have been calculated similar to those of Reference (2.), for polysulfone (density 1.370 g/cm ) spheres for values of n 4,6,8,10 (tetrahedral, primitive cubical, body-centered cubical, body-centered tetragonal geometries, respectively). Nitrogen vapor at -195.6°C was assumed and the adsorbed layer thickness was calculated with Halsey s equation (15) as in the cylindrical pore model. Calculated isotherms are plotted in Figure 5. [Pg.346]

For studies where the periodicity of the graphite surface plays a role in the determination of properties, (e.g., low-temperature determinations of the structure of layers adsorbed on graphite), the Fourier expanded molecule-surface potential of Steele is commonly used [4—6, 19]. For complex geometries such as heterogeneous surfaces (see Bojan et al., coal pores [20]) and fuUerenes [21] (Martinez-Alonso et al., Ar on C q), a fuU sum of the direct atom—atom potentials is needed. In the recent simulation studies of carbon nanotubes, some studies have used asummed atom-atom potential description (e.g., see the work of Stan et al. [22]) while others use a continuum cylindrical pore model [23, 24]. [Pg.81]

FIG. 2 Principles of SECMID using H+ as a model adsorbate. Schematic of the transport processes in the tip/substrate domain for a reversible adsorption/desorption process at the substrate following the application of a potential step to the tip UME where the reduction of H+ is diffusion-controlled. The coordinate system and notation for the axisymmetric cylindrical geometry is also shown. Note that the diagram is not to scale as the tip/substrate separation is typically <0.01 rs. [Pg.524]


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Cylindrical geometry

Model cylindrical

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