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Nonionized solutes

For gases, pure solids, pure liquids, and nonionic solutes, activity coefficients are approximately unity under most reasonable experimental conditions. For reactions involving only these species, differences between activity and concentration are negligible. Activity coefficients for ionic solutes, however, depend on the ionic composition of the solution. It is possible, using the extended Debye-Htickel theory, to calculate activity coefficients using equation 6.50... [Pg.173]

Adsorption is a physicochemical process whereby ionic and nonionic solutes become concentrated from solution at solid-liquid interfaces.3132 Adsorption and desorption are caused by interactions between and among molecules in solution and those in the structure of solid surfaces. Adsorption is a major mechanism affecting the mobility of heavy metals and toxic organic substances and is thus a major consideration when assessing transport. Because adsorption is usually fully or partly reversible (desorption), only rarely can it be considered a detoxification process for fate-assessment purposes. Although adsorption does not directly affect the toxicity of a substance, the substance may be rendered nontoxic by concurrent transformation processes such as hydrolysis and biodegradation. Many chemical and physical properties of both aqueous and solid phases affect adsorption, and the physical chemistry of the process itself is complex. For example, adsorption of one ion may result in desorption of another ion (known as ion exchange). [Pg.795]

Membrane uptake of nonionized solute is favored over that of ionized solute by the membrane/water partition coefficient (Kp). If Kp = 1 for a nonionized solute, membrane permeability should mirror the solute ionization curve (i.e., membrane permeability should be half the maximum value when mucosal pH equals solute pKa). When the Kp is high, membrane uptake of nonionized solute shifts the ionization equilibrium in the mucosal microclimate to replace nonionized solute removed by the membrane. As a result, solute membrane permeability (absorption rate) versus pH curves are shifted toward the right for weak acids and toward the left for weak bases (Fig. 7). [Pg.174]

Figure 1 gives the measurements of surface tension used for determining the CMCs of sulfonate/Genapol and nonylphenol 30 E.O. mixtures, with the last surfactant being called a desorbent (this term will be justified below). Minimum in surface tension was seen only for a few nonionic solutions (e.g. NP 50 E.O.). In this case, we used dyes that, once solubilized in the micelles, cause the solution to change color, which is another way of measuring the CMC. [Pg.278]

Ben-Naim, A. Marcus, Y., Solvation thermodynamics of nonionic solutes, J. Chem. Phys. 1984, 81, 2016-2027... [Pg.420]

The extent to which the ions compete with B for the charged sites (X) will determine their retention. In general, this type of chromatography may be used to separate ionic species, such as organic acids or bases, which can be ionized under certain pH conditions. Besides the reaction with ionic sites on the stationary phase, retention may also be affected by the partitioning of solutes between the mobile and stationary phases, as in reversed-phase chromatography. Thus, even nonionized solutes may be retained on ion-exchange columns. [Pg.523]

Since, for a nonionic solute B, we have -RT In % = AsoinG°, it follows that the temperature coefficient of its solubility is... [Pg.78]

Given a nonionic solute that has a relatively low solubility in each of the two liquids, and given equations that permit estimates of its solubility in each liquid to be made, the distribution ratio would be approximately the ratio of these solubilities. The approximation arises from several sources. One is that, in the ternary (solvent extraction) system, the two liquid phases are not the pure liquid solvents where the solubilities have been measured or estimated, but rather, their mutually saturated solutions. The lower the mutual solubility of the two solvents, the better can the approximation be made. Even at low concentrations, however, the solute may not obey Henry s law in one or both of the solvents (i.e., not form a dilute ideal solution with it). It may, for instance, dimerize or form a regular solution with an appreciable value of b(J) (see section 2.2). Such complications become negligible at very low concentrations, but not necessarily in the saturated solutions. [Pg.81]

Several models have been suggested for the estimation of the distribution ratios of nonionic solutes between water and (practically) immiscible organic solvents. One model takes 1-octanol to represent, in general, lipophilic ( fat-liking ) media, which hydrophobic ( water-fearing ) solutes would prefer over water. Such media may be oils, biological lipid membranes, and, somewhat less suitably, hydrocarbon solvents. [Pg.81]

When the acidity or the basicity of the solute molecule is high enough to stretch the OH or OD bond to the point of rupture, then the molecule dissociates into ions in solution. Therefore the dissociation constants also serve as a measure of acidity or basicity of solute molecules, especially those which are subject to significant ionization. Since the coulombic forces causing repulsion of ions at membrane-solution interfaces extend to distances farther than those involved in the polar hydrogen bonding repulsions of nonionized solutes at such interfaces, one would expect that a dissociated molecule to be repelled and, in... [Pg.31]

The parameters AVg (acidity), AVg (basicity), pK, and Zo represent properties of solute in the bulk solution phase. If reverse osmosis separation is governed by the property of solute in the membrane-solution interface, the existence of unique correlations between data on reverse osmosis separations and those on the above parameters, means that the property of solute in the bulk solution phase and the corresponding property of solute in the membrane-solution interface are also uniquely related. This leads one to the development of interfacial free energy parameters (-AAG/RT) for both nonionized solute molecules and dissociated ions in solution for reverse osmosis systems where water is preferentially sorbed at the membrane-solution interface. [Pg.32]

Fig. 1 Schematic representation of the separation principle of MEKC. An EOF/ micelle marker and three solutes differing in lipophilicity in the presence of anionic micelles in the background buffer are present. The lipophilicity increases in the sequence Sj < S2 < S3 t—migration time of EOF (nonionic solutes) S (solute) me —micelle. Fig. 1 Schematic representation of the separation principle of MEKC. An EOF/ micelle marker and three solutes differing in lipophilicity in the presence of anionic micelles in the background buffer are present. The lipophilicity increases in the sequence Sj < S2 < S3 t—migration time of EOF (nonionic solutes) S (solute) me —micelle.
The permeability of solutes across lipid bilayers is a product of the partition coefficient and the transverse diffusion coefficient [30]. Bilayer polymerization can alter solute diffusion by modifying either or both of these processes. In order to examine the effect of polymerization on bilayer permeability a nonionic solute of moderate permeability, [3H-glucose], was encapsulated in the vesicles prior to polymerization, removed from the exterior after polymerization, and its permeation across the bilayer was measured periodically [31]. Quantitative measurements of the 3H-glucose leakage revealed that the formation of linear polymer chains from methacryloyl lipids reduced the permeability coefficient to 0.3 to 0.5 of that of the unpolymerized lipid vesicles. A larger reduction (two orders of magnitude) was only found when crosslinked polymer networks were formed [31]. [Pg.60]

Another semiempirical relation has been suggested by Othmer and Thakar (03), which is also good only for dilute solutions of nonionic solutions the diffusion coefficient for a dilute solution of solute A in solvent B (in cm.2 sec.-1) is17... [Pg.198]

The potential at which the maximum occurs is different for different ions. In light of the third item, the differences in the voltage coordinates of the maxima must reflect differences in the chemical (as opposed to purely electrostatic) affinities of the ions for the interface. Nonionic solutes have also been investigated extensively, but we do not go into this aspect of the subject. [Pg.345]

Decreasing the degree of crosslinking will increase the water uptake for a mass of dry gel, though compromises in the efficiency will result. The effect of crosslinks on the separation of vitamin B-12, a nonionic solute of molecular weight 1355, is shown in Fig. 4 [16]. As the crosslink density decreases, the polymer chain length between crosslinks increases, yielding a looser structure which vitamin B-12 can more easily penetrate. The behavior fits well with the prediction from Flory excluded volume theory [16] ... [Pg.71]

ION EXCLUSION. The process in which a synthetic resin of ihc ion exchange type absorbs nonionized solutes such as glycerine or sugar while it docs not absorb inni/etl solutes that are also present in a solution in contact with the resin. Thus, sodium chloride and glycerine can he separated by passage of their aqueous solution through a bed of particles of an inn exclusion resin. [Pg.865]

Many water-insoluble drugs are either weak bases or weak acids. There exists an equilibrium of ionized and unionized species for a weak base or a weak acid in an aqueous solution. The pH car affect the equilibrium between ionized and nonionized solute species, and consequently can have an effect on the capacity of micellar solubility. An example of this is the decreased uptake of 4-chlorobenzoic acid by polysorbate 80 micelles observed when the pH is changed from 3 to 4.4 (Collette and Koo, 1975). Another example regarding the effect of SDS micelles orKthefp atenolol, nadolol, midazolam, and nitrazepam is provided by Castro et al. (1998). Apparent acidity constants (p of the drugs were determined potentiometrically or spectrophotometrically in... [Pg.276]

Thus, the limiting value of the slope of the curve of the temperature taken as a function of the molality is v times the value for a nonionic solute. [Pg.273]

List five ways of determining the activity coefficient of a nonionized solute. [Pg.283]

Obtained with low MW nonionic solute f Values found in published literature. [Pg.104]

As shown in Table 3.7, the osmotic pressure is high for various solutes. Ionic salts have a much higher pressure than nonionic solutes. Theoretically the osmotic pressure of an ionic salt is given by ... [Pg.164]

Solutes. Toluene, although polarizable, was chosen as an apolar solute. Caffeine was chosen as a polar but nonionic solute. Four ionic solutes were tested benzyltrimethylammonium bromide (BTAB) is a cationic quaternary ammonium salt. Benzoic acid acts as an anionic solute at mobile phase pH values between 5.5 and 6.5 (the pK lies between 3.7 in CTAB solutions and 4.7 in SDS solutions)(4). Sodium paraoctylbenzene sulfonate (SOBS) (pK -0.8) and cetylpyridinium chloride (CPC) were chosen as ionic solutes having surfactant properties. Their hydrophobic "tails have the same lenghts as those of SDS and CTAB, respectively. [Pg.132]

Table VI. values of the nonionic solutes. Experimental error 20%... Table VI. values of the nonionic solutes. Experimental error 20%...

See other pages where Nonionized solutes is mentioned: [Pg.193]    [Pg.128]    [Pg.201]    [Pg.467]    [Pg.117]    [Pg.19]    [Pg.144]    [Pg.91]    [Pg.91]    [Pg.193]    [Pg.1059]    [Pg.330]    [Pg.1016]    [Pg.16]    [Pg.23]    [Pg.31]    [Pg.34]    [Pg.223]    [Pg.57]    [Pg.468]    [Pg.36]    [Pg.236]    [Pg.139]    [Pg.331]    [Pg.136]    [Pg.137]   
See also in sourсe #XX -- [ Pg.52 ]




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Nonionic solutes

Nonionic solutions

Nonionic solutions

Nonionizing

Phase separation nonionic micellar solutions

Worm-Like Micelles in a Binary Solution of Nonionic Surfactant

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