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The transition region

The Transition Region For certain pore sizes, diffusion will not be purely molecular or purely Knudsen. Both types of diffusion will contribute to the overall flux. The theory for this transition region is complex. A workable approach is to assume that the two types of diffusion occur in parallel. This leads to [Pg.323]

The diffusion coefficient in the transition regime, Dp i, can depend on composition, as a result of the second term on the right-hand side of Eqn. (9-22), i.e., the resistance to molecular diffusion. The diffusion coefficient in the transition regime also depends on the pore radius, since Dp depends on pore radius. [Pg.323]

Concentration Dependence One important conclusion from the preceding discussion is that the diffiisivity in either the molecular or transition regime probably will depend on the mixture composition. However, the method that we developed for calculating the effectiveness factor is based on the assumption of a constant effective diffiisivity, independent of position and/or concentration. We might consider (very briefly ) resolving the basic differential equations that led to the effectiveness factor, for a concentration-dependent diffusion coefficient However, this would create a lot of additional complexity. Moreover, for many nonideal mixtures, the necessary relationships between the diffiisivities and concentration are not readUy available. Therefore, for a first-pass, an acceptable procedure is to use an average diffusion coefficient, calculated over the relevant range of concentration. Such a calculation is illustrated below. [Pg.323]

The irreversible cracking reaction CsHg C2H4 -h CH4 is taking place on the walls of a pore of radius r, in the presence of steam, an inert gas. The system is shown in the following figure. [Pg.323]

Let A denote propane (CsHg), B denote ethylene (C2H4), C denote methane (CH4), and I denote steam. The mole fractions of these components in the bulk gas stream, i.e., at the surface of the catalyst particle, are given in the following table, along with the values of the binary diffusivities. The values of r, T, and Ma are such that Z)A,k = 0-22 cm /s. An average value of Z)A,t is desired. [Pg.324]

For hard glassy materials the working range is often determined by the temperature spread between the brittle to tough transition and the main glass to rubber transition. [Pg.43]

since the end use of a polymeric material depends critically on the characteristics of the glass to rubber transition, we deal first with this phenomenon. [Pg.43]

The glass to rubber transition region is determined by the onset of conformational change involving internal rotation of the polymer main chain. The temperature midpoint of the change is called the glass transition temperature, T. There are several glass transition theories, but the one most closely related to the molecular motion approach is the kinetic theory. [Pg.43]

The glass to rubber transition occurs over a temperature range when the modulus drops from the high value characteristic of a glass to the unusually [Pg.43]


Keck J 1960 Variational theory of chemical reaction rates applied to three-body recombinations J. Chem. Phys. 32 1035 Anderson J B 1973 Statistical theories of chemical reactions. Distributions in the transition region J. Chem. Phys. 58 4684... [Pg.896]

In the reactant channel leading up to the transition region, motion along represents the FI atom approaching the molecule, while motion along / is the vibrational motion of the atom. The initial wavepacket is chosen to represent the desired initial conditions. In Figure 2, the FI2 molecule is initially in the ground... [Pg.260]

For Reynolds numbers > 1000, the flow is fully turbulent. Inertial forces prevail and becomes constant and equal to 0.44, the Newton region. The region in between Re = 0.2 and 1000 is known as the transition region andC is either described in a graph or by one or more empirical equations. [Pg.317]

Diffusion Flames in the Transition Region. As the velocity of the fuel jet increases in the laminar to turbulent transition region, an instabihty develops at the top of the flame and spreads down to its base. This is caused by the shear forces at the boundaries of the fuel jet. The flame length in the transition region is usually calculated by means of empirical formulas of the form (eq. 13) where I = length of the flame, m r = radius of the fuel jet, m v = fuel flow velocity, m/s and and are empirical constants. [Pg.519]

Transition Region Turbulent-flow equations for predicting heat transfer coefficients are usually vahd only at Reynolds numbers greater than 10,000. The transition region lies in the range 2000 < < 10,000. [Pg.562]

For velocity profiles in the transition region, see Patel and Head ]. Fluid Mech.,. 38, part 1, 181-201 [1969]) where profiles over the range 1,500 < Re < 10,000 are reported. [Pg.637]

Slip Flow In the transition region between molecular flow and continuum viscous flow, the conductance for fully developed pipe flow is most easily obtained by the method of Brown, et al. (J. Appl. Phys., 17, 802-813 [1946]), which uses the parameter... [Pg.641]

Often, a pilot plant will operate in the viscous region while the commercial unit will operate in the transition region, or alternatively, the pilot plant may be in the transition region and the commercial unit in the turbulent region. Some experience is required to estimate the difference in performance to be expected upon scale-up. [Pg.1625]

In the transition region [Reynolds numbers, Eq. (18-1), from 10 to 10,000], the width of the baffle may be reduced, often to one-half of standard width. If the circulation pattern is satisfactory when the tank is unbaffled but a vortex creates a problem, partial-length baffles may be used. These are standard-width and extend downward from the surface into about one-third of the liquid volume. [Pg.1628]

The usual practice in old wells of only partially cementing the outer pipe can lead to cell formation (steel in the cement-steel in the soil) in the transition regions to the uncoated sections (see Sections 4.2 and 4.3). In contrast to the well-known cathode steel-soil in the vicinity of the ground surface, the cathodic activity of the... [Pg.415]

In principle, energy landscapes are characterized by their local minima, which correspond to locally stable confonnations, and by the transition regions (barriers) that connect the minima. In small systems, which have only a few minima, it is possible to use a direct approach to identify all the local minima and thus to describe the entire potential energy surface. Such is the case for small reactive systems [9] and for the alanine dipeptide, which has only two significant degrees of freedom [50,51]. The direct approach becomes impractical, however, for larger systems with many degrees of freedom that are characterized by a multitude of local minima. [Pg.383]

Other Considerations In general, dry ESPs operate most efficiently with dust resistivities between 5x10 and 2 x lO ohm-cm. In general, the most diffieult particles to collect are those with aerodynamie diameters between 0.1 and 1.0 / m. Particles between 0.2 and 0.4 m usually show the most penetration. This is most likely a result of the transition region between field and diffusion charging. [Pg.421]

The distance from the top of the tube to the transition region is expressed ... [Pg.131]

Rules for which A is near Ac appear to support propagating solitoii structures, suggesting that the most complex rules (i.e. those belonging to Wolfram s class c4) lie within this transition region - A for Conway s Life rule, for example, is equal to 0.273 and lies within the transition region for k = 2, A/ = 9 two dimensional CA,... [Pg.100]

Numerical simulations of the k = oo case reveal a sharp phase transition at Ac = 0.27 [wootters]. Simulations also suggest that the spread in values of entropy decreases with increasing k, and that the width of the transition region probably goes as k f [woot90]. [Pg.106]

Class c4 rules characteristically have long transients, propagating soliton-like structures, large correlation lengths, etc. These are all properties possessed by rules within the transition region. [Pg.107]

Effective computation requires both the storage and transmission of information. If correlations between. separated sites aie too small, the sites evolve essentially independently of one another and little or no transmission of information takes place. On the other hand, if the correlations are too strong, distant sites may cooperate so strongly so as to effectively mimic each others behavior this, too, is not conducive to effective computation. It is only within the transition region that information can propagate freely over long distances without appreciable decay. [Pg.107]


See other pages where The transition region is mentioned: [Pg.47]    [Pg.380]    [Pg.601]    [Pg.1688]    [Pg.2267]    [Pg.2268]    [Pg.362]    [Pg.163]    [Pg.257]    [Pg.366]    [Pg.259]    [Pg.489]    [Pg.371]    [Pg.894]    [Pg.1623]    [Pg.1626]    [Pg.1631]    [Pg.379]    [Pg.483]    [Pg.70]    [Pg.111]    [Pg.112]    [Pg.93]    [Pg.265]    [Pg.280]    [Pg.310]    [Pg.311]    [Pg.11]    [Pg.282]    [Pg.99]    [Pg.106]    [Pg.107]    [Pg.107]    [Pg.402]   


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Breadth of the glass transition region

Electronic Transitions in the Critical Region

Photoselective chemistry access to the transition state region

Relationship between drag coefficient and Reynolds number in the transition region

Relaxation Activation Energy of Polymers in the Glass Transition Region

Separation in the Knudsen and Transition Regions

Spectroscopy in the transition state region

The Region

Thermodynamics in the region of glass transition

Transition region

Transitional regions

Viscous Flow and the Transition Region

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