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Sorbate species

In another study that underestimates the importance of carbon surface chemistry, Helmy et al. [709] set out to provide a pH/pK, relationship [that] permits the individual isotherms to be obtained for the charged and neutral sorbate species. They studied the uptakes of quinoline (pK = 4.9) and 8-hydroxyquinoline (pKa = 5.0) on a commercial charcoal the former reached a plateau as pH increased from 2 to 7, while the latter exhibited a maximum at pH = 6 and decreased thereafter. The authors theory led them to conclude that the surface of charcoal prefers the neutral over the charged molecule, which was confirmed by noting that their respective isotherms were of type I and type III. Intriguingly, the reasons for this preference were discussed only in terms of the repulsion between charged adsorbate species, while the electrostatic adsorbate-adsorbent interactions were ignored. Not surprisingly, the work of Muller and coworkers [523-525] is not cited. [Pg.331]

The closest approach to successful applications of polymer solution theory to humic substances was made by Chiou et al. (1983) when studying the binding of small organic chemicals by soils. They considered the soil sorbent substances to be amorphous macromolecular humic substances, and they adapted the Flory-Huggins theory to a study of the sorbate species solubilized in the amorphous macromolecules. [Pg.357]

Solving problems that involve the electrostatic adsorption models requires the solution of a number of simultaneous equations. These include intrinsic constant adsorption expressions (mass-action equations) such as just described, and mass- and material-balance and charge-balance equations that account for total surface sites and sorbate species associated with the surface and the solution (cf. Davis et al. 1978 Dzombak and Morel 1987 Allison et al. 1991). These equations are considered in more detail in discussions of the three models. [Pg.376]

Probably the TL model offers the most accurate description of the sorption process on an atomic scale. However, most published model parameters have been derived assuming that only H+ and OH occupy the zero plane and that all other sorbate species are found in the /0 plane (cf. Smith... [Pg.386]

What is the chemical composition and range of compositions of soil waters and what concentrations of sorbate species of interest are or might be present Does computer modeling of the water chemi.stry indicate that a potential sorbate species is at or above saturation with respect to a possible mineral Sorption of that species cannot be meaningfully examined, except at concentrations below mineral saturation. [Pg.392]

When multiple sorbent phases are present, which are most likely to interact with the sorbate species of interest ... [Pg.392]

Sverjensky (2003) proposed new standard states, leading to equilibrium constants independent of the surface area, site density, and the amount of the solid sorbent. These new standard states are dependent only on surface site occupancy and can be used with any surface complexation model. Different standard states are defined for the activities of the sorbent sites and the sorbate species. The theoretical relationships that apply for all adsorption reactions are developed below using Eq. (6.6) as an example reaction. [Pg.231]

Using these new standard states for the sorbent sites and sorbate species, the equilibrium constant for the surface protonation reaction, Eq. (6.6), is given by... [Pg.232]

An analytical expression for the breakthrough curve can be obtained by solving the equations describing continuity of a sorbate species in a fixed bed, the equilibrium relation between the solute and the sorbate, and the rate of adsorption and mass transfer, with the appropriate initial and boundary conditions. The exact solution of the complete set of equations is often impossible, but affinity chromatography lends itself to several convenient simplifications, with the result that analytical solutions are available. The notation used here is that of Vermeulen (4). [Pg.118]

The diffusivity of a liquid-phase reactant depends on its concentration (see Ruthven and Loughlin, 1971) and on the presence of other sorbate species. Although the concentration effect can be ignored in dilute solutions (as in gas-phase diffusion at all concentrations), it needs to be accounted for in concentrated solutions. Once the diffusivity is determined (usually by ignoring the effect of concentration), the effective diffusivity is best calculated from the relationship (Ternan, 1987, 1996)... [Pg.197]

H2 splitting over Ni (Eqs. (14.56) and (14.60)) can be described by the following adsorption isotherm as a function of the equilibrium constant, /CH,Ni> by assuming the formation of single-site sorbate species, that is, H-5 ... [Pg.326]


See other pages where Sorbate species is mentioned: [Pg.120]    [Pg.235]    [Pg.354]    [Pg.354]    [Pg.381]    [Pg.386]    [Pg.393]    [Pg.232]    [Pg.343]    [Pg.663]    [Pg.200]    [Pg.15]    [Pg.16]    [Pg.514]   


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Sorbate

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