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Fractional distribution

Since the void fraction distribution is independently measurable, the only remaining adjustable parameters are the A, so when surface diffusion is negligible equations (8.23) provide a completely predictive flux model. Unfortunately the assumption that (a) is independent of a is unlikely to be realistic, since the proportion of dead end pores will usually increase rapidly with decreasing pore radius. [Pg.75]

Analytical methods aie utilised by all branches of the chemical iadustry. Sometimes the goal is the quaUtative deterniiaation of elemental and molecular constituents of a selected specimen of matter othertimes the goal is the quantitative measurement of the fractional distribution of those constituents and sometimes it is to monitor a process stream or a static system. Information concerning the various iadividual analytical methods may be found ia separate articles dispersed alphabetically throughout the Eniyclopedia. The articles ate iatroductions to topics each of which is the subject of numerous books and other pubhcations. [Pg.393]

The mode occurs at the maximum in the differential mass fraction distribution curve. By differentiation and putting L = Lm at the mode. [Pg.73]

FIG. 4 Fractional distribution of solvent molecules oriented in a direction perpendicular to the plane of the wall across the length of the parallelepiped. Applied field as in Fig. 3 [26]. [Pg.788]

Eqs. (7)-(10) therein for determining fractional distributions of oxidation states for selected values of N (3[Pg.447]

The simplest way computationally of obtaining a sedimentation coefficient distribution is from time derivative analysis of the evolving concentration distribution profile across the cell [40,41]. The time derivative at each radial position r is d c r,t)/co /dt)r where cq is the initial loading concentration. Assuming that a sufficiently small time integral of scans are chosen so that Ac r t)/At= dc r t)ldt the apparent weight fraction distribution function g (s) n.b. sometimes written as (s ) can be calculated... [Pg.221]

Figure 5. Weight fraction distributions for polymer Seeds I ( ), 11 (A),... Figure 5. Weight fraction distributions for polymer Seeds I ( ), 11 (A),...
Calculated Molecular Weight Distributions. The calculated weight fraction distributions for the micro-mixed, segregated, and micro-mixed reactor with dead-polymer models for Runs 2, 5,... [Pg.316]

Figure 8. Comparison of experimental and calculated weight fraction distributions for Run 2 ((0) Exp (---------) Micro- D (---) Micro (---) Seg)... Figure 8. Comparison of experimental and calculated weight fraction distributions for Run 2 ((0) Exp (---------) Micro- D (---) Micro (---) Seg)...
Fig. 51.—Mole fraction distribution of chain molecules in a linear condensation polymer for several extents of reaction p. Fig. 51.—Mole fraction distribution of chain molecules in a linear condensation polymer for several extents of reaction p.
Fig. 55.—Weight fraction distribution of cyclic polymers for a type ii polymer with B Mo/c = 0.01 (g./cc.) as calculated from Eq. (16) for p =0.95 and 1.00 (solid curves) only even integral values of x apply. The chain distribution for p =0.95 is shown for comparison by the broken curve calculated from Eq. (3 ), p. 330. Fig. 55.—Weight fraction distribution of cyclic polymers for a type ii polymer with B Mo/c = 0.01 (g./cc.) as calculated from Eq. (16) for p =0.95 and 1.00 (solid curves) only even integral values of x apply. The chain distribution for p =0.95 is shown for comparison by the broken curve calculated from Eq. (3 ), p. 330.
Weight fraction distributions according to Eq. (33) for three values... [Pg.337]

With the aid of these results, the following are readily obtained. For the weight fraction distribution ... [Pg.367]

It will be observed that both of the distribution equations, (19) and (27) for the mole and weight fraction distributions, respectively, contain factors cox and Since a is limited to values less than Q c = l/(/— 1), is always much less than unity (for/=3 the maximum value of is j3c = l/4), and the factors o x and change in opposite directions as x increases. The decrease of the latter outweighs the increase of the former for all permissible values of see p. 366,... [Pg.367]

Fig. 69.—Weight fraction distribution for a branched polymer prepared from a simple trifunctional monomer at the a s indicated. ... Fig. 69.—Weight fraction distribution for a branched polymer prepared from a simple trifunctional monomer at the a s indicated. ...
For the purpose of deriving the weight fraction distribution, attention is directed to the fact that a molecule containing n /-functional branches is composed oi fn—n+1 chains. The average size of a chain being independent of the location of the chain in a branched structure, the quantity fn — n + 1 may be taken as a measure of the average weight of an n-chain polymer. It follows that... [Pg.396]

Denmark 1.5 days after the explosion. Air samples collected at Roskilde, Denmark on April 27-28, contained a mean air concentration of 241Am of 5.2 pBq/m3 (0.14 fCi/m3). In May 1986, the mean concentration was 11 pBq/m3 (0.30 fCi/m3) (Aarkrog 1988). Whereas debris from nuclear weapons testing is injected into the stratosphere, debris from Chernobyl was injected into the troposphere. As the mean residence time in the troposphere is 20-40 days, it would appear that the fallout would have decreased to very low levels by the end of 1986. However, from the levels of other radioactive elements, this was not the case. Sequential extraction studies were performed on aerosols collected in Lithuania after dust storms in September 1992 carried radioactive aerosols to the region from contaminated areas of the Ukraine and Belarus. The fraction distribution of241 Am in the aerosol samples was approximately (fraction, percent) organically-bound, 18% oxide-bound, 10% acid-soluble, 36% and residual, 32% (Lujaniene et al. 1999). Very little americium was found in the more readily extractable exchangeable and water soluble and specifically adsorbed fractions. [Pg.168]

W-3 CHF correlation. The insight into CHF mechanism obtained from visual observations and from macroscopic analyses of the individual effect of p, G, and X revealed that the local p-G-X effects are coupled in affecting the flow pattern and thence the CHF. The system pressure determines the saturation temperature and its associated thermal properties. Coupled with local enthalpy, it provides the local subcooling for bubble condensation or the latent heat (Hfg) for bubble formation. The saturation properties (viscosity and surface tension) affect the bubble size, bubble buoyancy, and the local void fraction distribution in a flow pattern. The local enthalpy couples with mass flux at a certain pressure determines the void slip ratio and coolant mixing. They, in turn, affect the bubble-layer thickness in a low-enthalpy bubbly flow or the liquid droplet entrainment in a high-enthalpy annular flow. [Pg.433]

Two parameters, the redistribution index (Uts) and the reduced partitioning parameter (IR), are used to describe the redistribution processes of trace elements in contaminated arid soils (Figs. 6.5-6.6) (Han et al., 2003a). The redistribution index depicts the removal or attainment of element-contaminated soils from or to the fractional distribution pattern characteristic of non-amended soils. However, the reduced partitioning parameter quantifies the relative binding intensity of trace elements in soils. [Pg.177]

Then, it is assumed that f, the fractional distribution of condensing isotopes on size interval i, can be derived from the measured Pb-212 distributions (i.e., the half-life of Po-218 is short enough that the distribution of daughter Pb-212 represents the initial fate of condensing species). [Pg.393]

However, in some special cases, the lost of information due to the thresholding procedure may cause a noticeable systematic error, because each lattice point such that < )(r) > < )0 contributes the same volume fraction 1/L3 regardless of the field magnitude. Consider an asymmetric binary mixture undergoing the phase separation. The local volume fraction distribution P(< >) has maxima at the equilibrium volume fractions, 1, and is asymmetric relatively to... [Pg.204]

FIGURE 11.3 Cobalt catalyst (for reaction conditions, see Figure 11.1) fraction distribution 1/distribution total fraction 13C incorporation. [Pg.203]

Fig Number-fraction distribution of chain molecules at different extents of reaction in polycondensation... [Pg.67]

Equation 2.8 relating the weight fraction distribution with the extent of reaction can also be used for determining the extent of reaction that should be attained to get a maximum yield of a particular Molecular weight species. Thus, from eq. (2.8) we can derive ... [Pg.67]

Around 1970 computer simulations of the branching processes on a lattice started to become a common technique. In bond percolation the following assessment is made [7] whenever two units come to lie on adjacent lattice sites a bond between the two units is formed. The simulation was made by throwing at random n units on a lattice with ISP lattice sites. Clusters of various size and shape were obtained from which, among others, the weight fraction distribution could be derived. The results could be cast in a form of [7]... [Pg.156]


See other pages where Fractional distribution is mentioned: [Pg.316]    [Pg.322]    [Pg.103]    [Pg.83]    [Pg.266]    [Pg.321]    [Pg.323]    [Pg.336]    [Pg.337]    [Pg.367]    [Pg.368]    [Pg.96]    [Pg.178]    [Pg.178]    [Pg.179]    [Pg.100]    [Pg.398]    [Pg.205]    [Pg.192]    [Pg.160]   
See also in sourсe #XX -- [ Pg.31 , Pg.254 ]




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