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Solute solution equilibrium

In studying the liquid-vapor equilibrium in Chapter 15 and the solute-solution equilibrium in Chapter 16, you learned that equilibrium exists when forward and reverse rates are the same in a reversible physical change. Similarly, in this chapter you will see that chemical equilibrium depends on the rates of chemical reactions. [Pg.528]

See any standard textbook on physical chemistry for more information on the Debye-Htickel theory and its application to solution equilibrium... [Pg.173]

Solute equilibrium parameters (X5,S for RPC and (Xz,Z for lEC Solute retention factor for initial mobile phase A ... [Pg.1537]

It was shown that most effective sorbents for concentration of heavy metals in water were silica-polyalumomethylsiloxane and its modified forms possessing increased capacity and the improved kinetic characteristics (solution equilibrium was attained within 5-10 min. for Pb(II) and Cd(II), 2-3 hours for Cu(II) and Zn(II), respectively). It was established that at joint presence of heavy metals in solutions over interval of concentrations 0,05-0,3 g/dm, possible at industrial accident and terrorist acts, the extraction of heavy metals by organoalumosiloxanes and their fonus modified by Cu(II) in water solutions accounted for 98,6-100 %. [Pg.440]

Figure 18.4 The hanging-drop method of protein crystallization, (a) About 10 pi of a 10 mg/ml protein solution in a buffer with added precipitant—such as ammonium sulfate, at a concentration below that at which it causes the protein to precipitate—is put on a thin glass plate that is sealed upside down on the top of a small container. In the container there is about 1 ml of concentrated precipitant solution. Equilibrium between the drop and the container is slowly reached through vapor diffusion, the precipitant concentration in the drop is increased by loss of water to the reservoir, and once the saturation point is reached the protein slowly comes out of solution. If other conditions such as pH and temperature are right, protein crystals will occur in the drop, (b) Crystals of recombinant enzyme RuBisCo from Anacystis nidulans formed by the hanging-drop method. (Courtesy of Janet Newman, Uppsala, who produced these crystals.)... Figure 18.4 The hanging-drop method of protein crystallization, (a) About 10 pi of a 10 mg/ml protein solution in a buffer with added precipitant—such as ammonium sulfate, at a concentration below that at which it causes the protein to precipitate—is put on a thin glass plate that is sealed upside down on the top of a small container. In the container there is about 1 ml of concentrated precipitant solution. Equilibrium between the drop and the container is slowly reached through vapor diffusion, the precipitant concentration in the drop is increased by loss of water to the reservoir, and once the saturation point is reached the protein slowly comes out of solution. If other conditions such as pH and temperature are right, protein crystals will occur in the drop, (b) Crystals of recombinant enzyme RuBisCo from Anacystis nidulans formed by the hanging-drop method. (Courtesy of Janet Newman, Uppsala, who produced these crystals.)...
The triarylmethyl cations are particularly stable because of the conjugation with the aryl groups, which delocalizes the positive charge. Because of their stability and ease of generation, the triarylmethyl cations have been the subject of studies aimed at determining the effect of substituents on carbocation stability. Many of these studies used the characteristic UV absorption spectra of the cations to determine their concentration. In acidic solution, equilibrium is established between triarylearbinols and the corresponding carbocations. [Pg.277]

This description of the dynamics of solute equilibrium is oversimplified, but is sufficiently accurate for the reader to understand the basic principles of solute distribution between two phases. For a more detailed explanation of dynamic equilibrium between immiscible phases the reader is referred to the kinetic theory of gases and liquids. [Pg.12]

The equation just written is generally applicable to any system. The equilibrium constant may be the K referred to in our discussion of gaseous equilibrium (Chapter 12), or any of the solution equilibrium constants (Rw Ra, Rj, K, . . . ) discussed in subsequent chapters. Notice that AG° is the standard free energy change (gases at 1 atm, species in solution at 1M). That is why, in the expression for K, gases enter as their partial pressures in atmospheres and ions or molecules in solution as their molarities. [Pg.467]

If the coexisting liquid or solid phases are not pure, but solutions, equilibrium will be established when the chemical potential... [Pg.376]

Figure 12-10 is a molecular view showing that the equilibrium concentration of a dissolved gas varies with the partial pressure of that gas. An increase in the partial pressure of gas results in an increase in the rate at which gas molecules enter the solution. This increases the concentration of gas in solution. The increased concentration in solution, in turn, results in an increase in the rate at which gas molecules escape from the solution. Equilibrium is reestablished when the solute concentration is high enough that the rate of escape equals the rate of capture. [Pg.851]

Fig. 2.7. Relation between the pH and CP concentration of geothermal waters. The solid line indicates the albite-K-feldspar-muscovite-quartz-solution equilibrium at 250°C. For symbols used see caption to Fig. 2.2. (Shikazono, 1978a). Fig. 2.7. Relation between the pH and CP concentration of geothermal waters. The solid line indicates the albite-K-feldspar-muscovite-quartz-solution equilibrium at 250°C. For symbols used see caption to Fig. 2.2. (Shikazono, 1978a).
Fig. 2.8. Relation between the Ca and CR concentrations of geothermal waters and inclusion fluids. Solid lines indicate (1) albite-K-feldspar-muscovite-quartz-caleite-solution equilibrium at OHaCOs = 10 (2) albite-K-feldspar-muscovite-quartz-calcite-solution equilibriumn at oh2C03 = 10 (3) anhydrite-solution at SSo (total dissolved sulfate concentration) = 10 and (4) anhydrite-solution equilibrium at SSq = 10. For symbols used see caption to Fig. 2.2 (Shikazono, 1978a). Fig. 2.8. Relation between the Ca and CR concentrations of geothermal waters and inclusion fluids. Solid lines indicate (1) albite-K-feldspar-muscovite-quartz-caleite-solution equilibrium at OHaCOs = 10 (2) albite-K-feldspar-muscovite-quartz-calcite-solution equilibriumn at oh2C03 = 10 (3) anhydrite-solution at SSo (total dissolved sulfate concentration) = 10 and (4) anhydrite-solution equilibrium at SSq = 10. For symbols used see caption to Fig. 2.2 (Shikazono, 1978a).
The Na/Li ratio of geothermal waters decreases with increasing temperature and has been used as a geothermometer (Fig. 2.10) (Fouillac and Michard, 1981), suggesting that this ratio is controlled by feldspar-solution equilibrium (Shikazono, 1978a). [Pg.302]

Fig. 2.14. The variation of concentration of with concentration of CP in aqueous solution in equilibrium with a given mineral assemblage at 250°C. I Equilibrium curve based on albite-sericite-Na-montmorillonite-quartz-aqueous solution equilibrium and Na-K-Ca relationship obtained by Fournier and Truesdell (1973). 2 Equilibrium curve based on albite-K-feldspar-aqueous solution equilibrium and Na-K-Ca relationship obtained by Fournier and Truesdell (1973). 3 Wairakite-albite-sericite-K-feldspar-quartz. 4 Calcite-albite-sericite-K-feldspar-quartz (/jjhjCO, = 10 ). 5 Calcite-albite-sericite-Na-montmorillonite-quartz (mH2C03 = 10 ). 6 Ca-montmorillonite-albite-sericite-Na-montmorillonite-quartz. 7 Calcite-albite-sericite-K-feld-spar-quartz (mnjCOj = 10 ). 8 Calcite-albite-sericite-Na-montmorillonite-quartz (mHjCOj = 10 ). 9 Ca-montmorillonite-albite-sericite-K-feldspar-quartz. 10 Anhydrite = 10 ). (Shikazono, 1976)... Fig. 2.14. The variation of concentration of with concentration of CP in aqueous solution in equilibrium with a given mineral assemblage at 250°C. I Equilibrium curve based on albite-sericite-Na-montmorillonite-quartz-aqueous solution equilibrium and Na-K-Ca relationship obtained by Fournier and Truesdell (1973). 2 Equilibrium curve based on albite-K-feldspar-aqueous solution equilibrium and Na-K-Ca relationship obtained by Fournier and Truesdell (1973). 3 Wairakite-albite-sericite-K-feldspar-quartz. 4 Calcite-albite-sericite-K-feldspar-quartz (/jjhjCO, = 10 ). 5 Calcite-albite-sericite-Na-montmorillonite-quartz (mH2C03 = 10 ). 6 Ca-montmorillonite-albite-sericite-Na-montmorillonite-quartz. 7 Calcite-albite-sericite-K-feld-spar-quartz (mnjCOj = 10 ). 8 Calcite-albite-sericite-Na-montmorillonite-quartz (mHjCOj = 10 ). 9 Ca-montmorillonite-albite-sericite-K-feldspar-quartz. 10 Anhydrite = 10 ). (Shikazono, 1976)...
However, if there was sufficient amount of H+ ions in the solution, equilibrium shifted towards the left and bismuth remained in the solution as Bi3+. Therefore, during sonication activated water molecules were formed which reacted with Bi3+ ions. But instead of forming Bi(OH)3, they formed bismuthyl ions, BiO+, due to the fact that Bi(OH)3 was a weaker base, therefore hydrolysed readily to generate bismuthyl ion, BiO+. These steps could be summarised as under ... [Pg.251]

If it is assumed that in more concentrated solutions the rate of the forward reaction continues to follow this rate expression, what forms of the reverse rate are thermodynamically consistent in concentrated acid solution Equilibrium is to be established with respect to equation A when written in the N204 form. It may be assumed that the dependence on N02 and N204 concentrations may be lumped together by equation C. [Pg.138]

Hartley, F. R., Burgess, C. Alcock, R., Solution Equilibrium, Ellis Horwood Chichester, 1980. [Pg.47]

Potentiometric EDTA titrations are best carried out with a mercury pool electrode (Figure 5.6) or a gold amalgam electrode. When this electrode dips into a solution containing the analyte together with a small amount of added Hg-EDTA complex, three interdependent reactions occur. For example, at pH = 8 the half cell reaction (a) which determines the electrode potential is related to the solution equilibrium by (b) and (c). [Pg.212]

PROFILE is a biogeochemical model developed specially to calculate the influence of acid depositions on soil as a part of an ecosystem. The sets of chemical and biogeochemical reactions implemented in this model are (1) soil solution equilibrium, (2) mineral weathering, (3) nitrification and (4) nutrient uptake. Other biogeochemical processes affect soil chemistry via boundary conditions. However, there are many important physical soil processes and site conditions such as convective transport of solutes through the soil profile, the almost total absence of radial water flux (down through the soil profile) in mountain soils, the absence of radial runoff from the profile in soils with permafrost, etc., which are not implemented in the model and have to be taken into account in other ways. [Pg.51]

Soil solution equilibrium. Soil solution equilibriumis based on the quantification of acid-neutralizing capacity, ANC, which has been defined as ... [Pg.51]

With these insights on the meaning of s3, we now outline a possible outcome of the ESP analysis for the two VB state picture of the BuCl Svl dissociation. Let us imagine following the reaction from the solute equilibrium geometry, where the BuCl system is largely electronically localized in the covalent state 2>. It is reasonable to expect that the product of the... [Pg.275]

The maximum preconcentration advantage for an ionomer-film-modified electrode is obtained with ionomer-film-analyte solution equilibrium is... [Pg.100]

For the molecular solute, equilibrium between the vapor phase and the liquid phase is given by ... [Pg.51]

Other references in Table in discuss applications in precipitation of metal.compounds, gaseous reduction of metals from solution, equilibrium of copper in solvent extraction, electrolyte purification and solid-liquid equilibria in concentrated salt solutions. The papers by Cognet and Renon (25) and Vega and Funk (59) stand out as recent studies in which rational approaches have been used for estimating ionic activity coefficients. In general, however, few of the studies are based on the more recent developments in ionic activity coefficients. [Pg.637]

Similarly, for the system of iron/calcium/phosphate, the percentage distribution of various complexes can also be calculated using solution equilibrium calculations as shown in Fig. 6.26. It follows that depending on solution pH, the dominant complexes is CaPO at pH= 10, whereas CaHP04(aq) and CaH2P04are dominant at pH = 8. [Pg.163]

To reestablish equilibrium, p g must be decreased also. This decrease in p can be accomplished by decreasing the temperature. The chemical potential of the liquid solvent is decreased by the drop in temperature as well as by the addition of solute. Equilibrium is reestablished if... [Pg.350]

The hydrotropic action of a dicarboxylic acid is discussed against the general features of hydro-tropic action the liquid crystal/isotropic solution equilibrium. It is shown that the hydrotropic action of the dicarboxylic acid in question, 8-[5(6)-carboxy-4-hexyl-cyclohex-2-enyl] octanoic acid, depends on its conformation at an interface. [Pg.107]


See other pages where Solute solution equilibrium is mentioned: [Pg.505]    [Pg.364]    [Pg.174]    [Pg.10]    [Pg.51]    [Pg.368]    [Pg.303]    [Pg.852]    [Pg.402]    [Pg.6]    [Pg.307]    [Pg.198]    [Pg.103]    [Pg.466]    [Pg.67]    [Pg.29]    [Pg.36]    [Pg.77]    [Pg.1]    [Pg.16]   
See also in sourсe #XX -- [ Pg.323 ]




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