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Diffusive phenomena

The overall extraction process is sometimes subdivided into two general categories according to the main mechanisms responsible for the dissolution stage (/) those operations that occur because of the solubiHty of the solute in or its miscibility with the solvent, eg, oilseed extraction, and (2) extractions where the solvent must react with a constituent of the soHd material in order to produce a compound soluble in the solvent, eg, the extraction of metals from metalliferous ores. In the former case the rate of extraction is most likely to be controUed by diffusion phenomena, but in the latter the kinetics of the reaction producing the solute may play a dominant role. [Pg.87]

In many process design applications like polymerization and plasticization, specific knowledge of the thermodynamics of polymer systems can be very useful. For example, non-ideal solution behavior strongly governs the diffusion phenomena observed for polymer melts and concentrated solutions. Hence, accurate modeling of... [Pg.17]

In addition to the insoluble polymers described above, soluble polymers, such as non-cross-linked PS and PEG have proven useful for synthetic applications. However, since synthesis on soluble supports is more difficult to automate, these polymers are not used as extensively as insoluble beads. Soluble polymers offer most of the advantages of both homogeneous-phase chemistry (lack of diffusion phenomena and easy monitoring) and solid-phase techniques (use of excess reagents and ease of isolation and purification of products). Separation of the functionalized matrix is achieved by either precipitation (solvent or heat), membrane filtration, or size-exclusion chromatography [98,99]. [Pg.87]

Figure 2.12 shows the rate, the coverages, the reaction orders, and the normalized apparent activation energy, all as a function of temperature. Note the strong variations of all these parameters with temperature, in particular that of the rate, which initially increases, then maximizes and decreases again at high temperatures. This characteristic behavior is expected for all catalytic reactions, but is in practice difficult to observe with supported catalysts because diffusion phenomena come into play. [Pg.67]

The same property of entropy generation holds for other processes. In electrical conductance, charged particles move from higher to lower electrical potentials. In diffusion phenomena, all chemical entities are transferred from higher to lower chemical potentials. [Pg.119]

To summarize, there is a sizable and self-consistent body of data indicating that rotational and translational mobility of molecules inside swollen gel-type CFPs are interrelated and controlled mainly by viscosity. Accordingly, T, self-diffusion and diffusion coefficients bear the same information (at least for comparative purposes) concerning diffusion rates within swollen gel phases. However, the measurement of r is by far the most simple (it requires only the collection of a single spectrum). For this reason, only r values have been used so far in the interpretation of diffusion phenomena in swollen heterogeneous metal catalysts supported on CFPs [81,82]. [Pg.222]

Restricted diffusion, correlated motion of spins, or any deviation from a free behavior of the molecules will result in a propagator shape different from a Gaussian one. A wide range of studies have dealt with such problems during the last two decades and NMR has turned out to be the method of choice for quantifying restricted diffusion phenomena such as for liquids in porous materials or dynamics of entangled polymer molecules. [Pg.24]

FA Long, D Richman. Concentration gradients for diffusion of vapors in glassy polymers and their relation to time dependent diffusion phenomena. J Am Chem Soc 82 513-522, 1960. [Pg.553]

When it occurs, the adsorption on reactive sites, located in shielded areas, may therefore occur after less reactive sites, better exposed, have reacted. Diffusion may thus cause the smoothing out of significant details in the energy spectrum and the Q-d curves, determined in the presence of diffusion phenomena, indicate less surface heterogeneity than actually exists on the adsorbent surface. [Pg.243]

As the pore size is reduced to 1 nm or less, gas permeation may exhibit a thermally activated diffusion phenomena. For example, in studies at Oak Ridge National Laboratory, for a certain proprietary membrane material and configuration, permeation of helium appeared to increase much faster than other gases resulting in an increase in Helium to C02 selectivity from 5 at 25°C to about 48.3 at 250°C (Bischoff and Judkins, 2006). Hydrothermal stability of this membrane in the presence of steam, however, was not reported. [Pg.308]

Modeling of pore diffusion phenomena can be a helpful tool mainly in terms of catalyst design considerations but also in terms of understanding the effects caused by diffusional restrictions. For example, a modeling study by Wang et al.7 demonstrated a negative impact on selectivity by particle diffusion limitations. [Pg.216]

Fig. 6 Correlation curve showing the various processes that occur in different time regimes. Supramolecular dynamics can be measured in any of the time regimes between the antibunching and diffusion phenomena. Fig. 6 Correlation curve showing the various processes that occur in different time regimes. Supramolecular dynamics can be measured in any of the time regimes between the antibunching and diffusion phenomena.
This kind of mean diameter is pertinent in connection with diffusion phenomena since surface is the major factor then. [Pg.745]

Impedances of Real Cells Quantification of Diffusion Phenomena and the Warburg Impedance... [Pg.262]

In systems where diffusion phenomena are of significance, the mechanistic study is facilitated by using the general expression for Impedance Z (26). This equation shows for instance how the Warburg coefficient can be evaluated by conducting impedance studies at very low frequencies. These coefficients in turn enable the evaluation of diffusion coefficients for the diffusing species. [Pg.60]

Appearance of Warburg-type behavior shows that diffusion phenomena become predominant In some coatings as their deterioration progresses. [Pg.75]

The width of a peak, or, in other words, the length of a solute zone, is affected primarily by diffusion phenomena leading to a broadening of the solute zone. In addition, in capillary zone electrophoresis, zone broadening can be caused by thermal effects, electrodispersion, or adsorptive effects. All these effects can be expressed as coefficients of variance cr2, adding to a total coefficient of variance of the system ofotal ... [Pg.25]


See other pages where Diffusive phenomena is mentioned: [Pg.802]    [Pg.510]    [Pg.70]    [Pg.179]    [Pg.225]    [Pg.219]    [Pg.220]    [Pg.222]    [Pg.206]    [Pg.234]    [Pg.267]    [Pg.562]    [Pg.14]    [Pg.244]    [Pg.238]    [Pg.337]    [Pg.417]    [Pg.345]    [Pg.119]    [Pg.63]    [Pg.242]    [Pg.254]    [Pg.176]    [Pg.168]    [Pg.369]    [Pg.248]    [Pg.10]    [Pg.11]    [Pg.480]    [Pg.367]    [Pg.72]    [Pg.224]    [Pg.214]    [Pg.132]   
See also in sourсe #XX -- [ Pg.3 , Pg.30 ]




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Back-diffusion, phenomenon

Diffusion phenomena

Dyeing process diffusion phenomena

Dynamical diffusion phenomena

Internal diffusion phenomena

Mass transport phenomena Diffusion

Surface phenomena diffusion

The Phenomena of Diffusion

The Phenomenon of Hydrodynamic Diffusion

The diffusion phenomenon

Transport phenomena diffusion

Transport phenomena diffusion-controlled

Transport phenomena molecular diffusion

Variation of the sample profile along its travel convective and diffusive phenomena

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