Diffusion adsorbents

This effect is well-known in synthetic polymer adsorption and results in low molecular weight species (fast diffusion) adsorbed initially, but the high molecular weight fractions are preferentially adsorbed at very long times (higher adsorption free energy) (see Fig. 22). 

Species A arrives at the interface by convective diffusion, adsorbs and reacts, producing species P (see Fig. 4-2). 

Then there is surface diffusion. Adsorbed ions and radicals arrive on adsorbing sites and their ability to get away from them to active catalytic sites is determined by surface diffusion on the various faces of critical surface. Obviously, all this occurs under high electric field strengths, which will change with the chosen potential at which the reaction is to be run. 

One potential drawback of devices in which adsorption occurs on a deep bed of catalyst packed in an MAS rotor is the occurrence of a nonuniform distribution of reactant. This problem is illustrated by the Cs MAS spectra of zeolite CsZSM-5 in Fig. 5 [47]. Without adsorbates, the Cs chemical shift was —157 ppm at 298 K. An amount of methanol- C equivalent to 1 methanol molecule for every Cs in the zeolite was then introduced using the apparatus in Fig. 4, and the spectrum in Fig. 5b was obtained. The spectrum shows the consequences of a deep-bed adsorption of a slowly diffusing adsorbate. Rather than a single Cs resonance reflecting the adsorption of one equivalent of the methanol, there are two signals one at — 157 ppm originating from the bottom of the catalyst bed and a second at — 82 ppm from the top of the catalyst bed. The... 

Surfaces are heterogeneous on the atomic scale. Atoms appear in flat terraces, at steps, and at kinks. There are also surface point defects, vacancies, and adatoms. These various surface sites achieve their equilibrium surface concentrations through an atom-transport process along the surface that we call surface diffusion. Adsorbed atoms and molecules reach their equilibrium distribution on the surface in the same way. This view of surface diffusion as a site-to-site hopping process leads to the random-walk picture, in which the mean-square displacement of the adsorbed particle along the. r-component of the coordinate is given by... 

Surface diffusion adsorbed species on the walls of the pores may be transported along the pore walls. This mechanism is important for strongly adsorbed species and in micro-pores. 

When the solid/liquid and liquid/air surfaces have a stronger affinity toward the polymer than toward the solvent, a diffuse adsorbed layer is formed. The size of this layer is related to the radius of the polymer coils and is typically 100 A for a molecular weight of 10. Here again, the result is a long-range interaction that is (most often) repulsive." ... 

The scaling theory, based on the power laws, allows one to predict that long flexible chains, adsorbed at the solid surface, build self-similar diffuse adsorbed layers. 

Equilibrium separation factors depend upon the nature of the adsorbate -adsorbent interactions, that is, on whether the surface is polar, non-polar, hydrophilic, hydrophobic, etc. and on the process conditions such as temperature, pressure and concentration. Kinetic separations are generally, but not exclusively, possible only with molecular sieve adsorbents such as zeolites and carbon sieves. The kinetic selectivity in this case is largely determined by the ratio of micropore diffusivities of the components being separated. For a useful separation to be based on kinetics the size of the adsorbent micropores must be comparable with the dimensions of the diffusing adsorbate molecules. 

IHP) (the Helmholtz condenser formula is used in connection with it), located at the surface of the layer of Stem adsorbed ions, and an outer Helmholtz plane (OHP), located on the plane of centers of the next layer of ions marking the beginning of the diffuse layer. These planes, marked IHP and OHP in Fig. V-3 are merely planes of average electrical property the actual local potentials, if they could be measured, must vary wildly between locations where there is an adsorbed ion and places where only water resides on the surface. For liquid surfaces, discussed in Section V-7C, the interface will not be smooth due to thermal waves (Section IV-3). Sweeney and co-workers applied gradient theory (see Chapter III) to model the electric double layer and interfacial tension of a hydrocarbon-aqueous electrolyte interface [27]. 

It is necessary that the mercury or other metallic surface be polarized, that is, that there be essentially no current flow across the interface. In this way no chemical changes occur, and the electrocapillary effect is entirely associated with potential changes at the interface and corresponding changes in the adsorbed layer and diffuse layer. 

NMR Nuclear magnetic resonance [223, 224] Chemical shift of splitting of nuclear spin states in a magnetic field H [225], C [226, 227], N [228], F [229], 2 Xe [230] Other Techniques Chemical state diffusion of adsorbed species... 

Alternative approaches treat the adsorbed layer as an ideal solution or in terms of a Polanyi potential model (see Refs. 12-14 and Section XVII-7) a related approach has been presented by Myers and Sircar [15]. Adsorption rates have been modeled as diffusion controlled [16,17]. 

Protein adsorption has been studied with a variety of techniques such as ellipsome-try [107,108], ESCA [109], surface forces measurements [102], total internal reflection fluorescence (TIRE) [103,110], electron microscopy [111], and electrokinetic measurement of latex particles [112,113] and capillaries [114], The TIRE technique has recently been adapted to observe surface diffusion [106] and orientation [IIS] in adsorbed layers. These experiments point toward the significant influence of the protein-surface interaction on the adsorption characteristics [105,108,110]. A very important interaction is due to the hydrophobic interaction between parts of the protein and polymeric surfaces [18], although often electrostatic interactions are also influential [ 116]. Protein desorption can be affected by altering the pH [117] or by the introduction of a complexing agent [118]. 

The interaction of an electrolyte with an adsorbent may take one of several forms. Several of these are discussed, albeit briefly, in what follows. The electrolyte may be adsorbed in toto, in which case the situation is similar to that for molecular adsorption. It is more often true, however, that ions of one sign are held more strongly, with those of the opposite sign forming a diffuse or secondary layer. The surface may be polar, with a potential l/, so that primary adsorption can be treated in terms of the Stem model (Section V-3), or the adsorption of interest may involve exchange of ions in the diffuse layer. 

The state of an adsorbate is often described as mobile or localized, usually in connection with adsorption models and analyses of adsorption entropies (see Section XVII-3C). A more direct criterion is, in analogy to that of the fluidity of a bulk phase, the degree of mobility as reflected by the surface diffusion coefficient. This may be estimated from the dielectric relaxation time Resing [115] gives values of the diffusion coefficient for adsorbed water ranging from near bulk liquids values (lO cm /sec) to as low as 10 cm /sec. 

The sequence of events in a surface-catalyzed reaction comprises (1) diffusion of reactants to the surface (usually considered to be fast) (2) adsorption of the reactants on the surface (slow if activated) (3) surface diffusion of reactants to active sites (if the adsorption is mobile) (4) reaction of the adsorbed species (often rate-determining) (5) desorption of the reaction products (often slow) and (6) diffusion of the products away from the surface. Processes 1 and 6 may be rate-determining where one is dealing with a porous catalyst [197]. The situation is illustrated in Fig. XVIII-22 (see also Ref. 198 notice in the figure the variety of processes that may be present). 

The Langmuir-Hinshelwood picture is essentially that of Fig. XVIII-14. If the process is unimolecular, the species meanders around on the surface until it receives the activation energy to go over to product(s), which then desorb. If the process is bimolecular, two species diffuse around until a reactive encounter occurs. The reaction will be diffusion controlled if it occurs on every encounter (see Ref. 211) the theory of surface diffusional encounters has been treated (see Ref. 212) the subject may also be approached by means of Monte Carlo/molecular dynamics techniques [213]. In the case of activated bimolecular reactions, however, there will in general be many encounters before the reactive one, and the rate law for the surface reaction is generally written by analogy to the mass action law for solutions. That is, for a bimolecular process, the rate is taken to be proportional to the product of the two surface concentrations. It is interesting, however, that essentially the same rate law is obtained if the adsorption is strictly localized and species react only if they happen to adsorb on adjacent sites (note Ref. 214). (The apparent rate law, that is, the rate law in terms of gas pressures, depends on the form of the adsorption isotherm, as discussed in the next section.)... 

Gomer R 1990 Diffusion of adsorbates on metai surfaces Rep. Prog. Phys. 53 917... 

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