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Concentration excess components

For a single equation, Eqs. (7-36) and (7-37) relate the amounts of the several participants. For multiple reactions, the procedure for finding the concentrations of all participants starts by assuming that the reactions proceed consecutively. Key components are identified. Intermediate concentrations are identified by subscripts. The resulting concentration from a particular reaction is the starting concentration for the next reaction in the series. The final value carries no subscript. After the intermediate concentrations are ehminated algebraically, the compositions of the excess components will be expressible in terms of the key components. [Pg.690]

Process Objective UF is used for three principle objectives. First, to fractionate, to pass selectively one component through the membrane with the solvent. Second, to concentrate, to pass the solvent. These two, while different, are related and it is common to purify and concentrate a component siiTuiltaneously. The third objective, quite different, is to produce a solvent stream as a product. An example is the operation of an ultrafilter for producing low-cost permeate. An important apphcation of UF is in the automotive industiy where UF is used to remove water and microsolutes from huge electrophoretic paint tanks for use in rinsing excess paint (dragout) from... [Pg.2041]

Investigations on phase ratio are also useful. This does not only affect partition and concentration of components (both water-soluble and poorly water-soluble), but also reduces the reaction inhibition by the product, the substrate excess or any other chemical inhibitor [37,40]. [Pg.556]

Figure D3.5.2 Definition of the Gibbs dividing plane based on the excess concentration of component A of the two phases a and p that are in direct contact with each other. Figure D3.5.2 Definition of the Gibbs dividing plane based on the excess concentration of component A of the two phases a and p that are in direct contact with each other.
In treating interfacial (if) regions, we will follow the method of Gibbs and replace the nonuniform interfacial region by a two-dimensional Gibbs surface phase with uniform properties. Properties of this phase are called surface excess properties and their calculation is illustrated for the surface excess concentration of component i in Fig. 8. Here, the actual interfacial region, the region where properties vary, extends from zj to z2 and is replaced by the surface phase located at position z0, with the uniform bulk a and (1 phases extended up to this position. [Pg.335]

The concentration of excess components in precipitation is the difference between the total concentration and the sea-salt component of the total concentration. There are often large uncertainties associated with excess concentrations resulting from small differences between large numbers. Hawley, Galloway, and Keene (University of Virginia, Charlottesville, unpublished data) have derived a nomogram technique to determine the uncertainty involved knowing only the total concentration of the element in question (e.g., S04 ), the total Na+ concentration, and the respective analy-... [Pg.49]

Similariy, the excess concentration of component 1 in the solvation shell of the anions is... [Pg.140]

Now, the key thermodynamic aspects of this mechanism (reviewed in [4,78,79]) will be examined in more detail. Setting component 1 = principal solvent (here water), component 2 = protein, and component 3 = solute (e.g., sucrose or PEG), the preferential interaction of component 3 with a protein is expressed, within close approximation, by the parameter (5m3/5m2) jj at constant temperature and pressure, where p, and m, are the chemical potential and molal concentration of component /, respectively. A positive value of this interaction parameter indicates an excess of component 3 in the vicinity of the protein over the bulk concentration (i.e., preferential binding of the solute). A negative value for this parameter indicates a deficiency of component 3 in the protein domain. Component 3 (the solute) is preferentially excluded and component 1 (water) is in excess in the protein domain. [Pg.148]

The type IV plot is similar to type 111, but the surface excess concentration of component 1, Tj , becomes negative at high concentrations, before returning to zero. The plot is quite imsymmetrical. In type V, the curve Intersects the concentration axis toward the center of the graph and is closer to symmetrical. [Pg.80]

In general, the choice of the position of the Gibbs dividing surface is arbitrary. It is possible to define quantities which are invariant with respect to the choice of its location. If Fj or Fj, are the relative adsorption and F and Ff the Gibbs surface excess concentrations of components i and 1, respectively, then the relative adsorption of component i with respect to component 1 is defined by... [Pg.40]

At least one exception in the organotin mercaptides has been noted. In the dimethyltin di( benzyl mercaptide )/dimethyltin dichloride system, regardless of the relative concentrations used, the NMR spectra consisted of broad lines and did not contain any resonances characteristic of the excess component. At 25°C, the reaction appears to be one involving a rapid equilibrium exchange of groups (14). However, at about — 10°C, the resonances of the individual components can be observed owing to a slow rate of exchange (15). [Pg.374]

An even simpler system composed of dibutyltin diacetate and dibutyltin dichloride was examined by both 13C NMR and low-temperature XH NMR because of the report that dibutylchlorotin acetate formed immediately when the reagents were mixed in carbon tetrachloride (16). The 13C spectra of the pure diacetate and the mixed system were obtained using conditions suitable for quantitative analysis. In deuterochloroform, at 30 °C, over a wide range of concentrations, no evidence could be found for the presence of the excess component or the exclusive formation of dibutylchlorotin acetate. The 1H NMR spectra gave similar results and the spectra were unchanged between 50° and — 50° C. [Pg.375]

Surface Excess Isotherm A function relating, at constant temperature and pressure, the relative adsorption, reduced adsorption, or similar surface excess quantity to the concentration of component in the equilibrium bulk phase. [Pg.521]

The reason for defining the reference system is that the properties of the interface are governed by excesses and deficiencies in the concentrations of components that is, we are concerned with differences between the quantities of various species in the actual interfacial region, with respect to the quantities we would expect if the existence of the interface did not perturb the pure phases, a and j8. These differences are called surface excess quantities. For example, the surface excess in the number of moles of any species, such as potassium ions or electrons, would be... [Pg.535]

For the mechanisms depicted above (Eqns. 10-12) and where B is the component in excess, the concentration of component A follows Eqn. 13. [Pg.116]

In addition, DC polarography has a more specific limitation. Measurement of a more positive wave in the presence of an excess of material reduced at more negative potentials (wave A in Fig. 3.14) can be carried out with maximum accuracy but when the trace material to be determined is reduced at more negative potentials (wave B in Fig. 3.14)—that is, when a small wave follows a large one—measurement of the small, more negative, wave can be carried out only when the concentration ratio between the excess component and the analyzed species is less than about 10 1. At larger excess the accuracy of the determination of the trace component decreases considerably. [Pg.71]

Covering the melt is usually not possible in large commercial melting tanks. It may be necessary to allow for losses by providing excess concentrations of components known to vaporize from a given melt. This procedure is quite efficient for continuous melting of a constant composition, where analysis of the product over a period of time can be used to establish the exact amount of excess component needed to counter the volatilization losses. In a few cases, it may be possible to... [Pg.38]

The difference between the amount adsorbed, n, and the surface excess, n, is important in some cases but may be negligible in others. On one hand, for a low concentration of component 1 ... [Pg.678]


See other pages where Concentration excess components is mentioned: [Pg.251]    [Pg.204]    [Pg.60]    [Pg.81]    [Pg.154]    [Pg.122]    [Pg.148]    [Pg.116]    [Pg.238]    [Pg.51]    [Pg.1536]    [Pg.94]    [Pg.115]    [Pg.778]    [Pg.108]    [Pg.116]    [Pg.624]    [Pg.286]    [Pg.680]    [Pg.101]    [Pg.246]    [Pg.591]    [Pg.313]    [Pg.156]    [Pg.148]   
See also in sourсe #XX -- [ Pg.43 , Pg.44 , Pg.45 , Pg.46 ]




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Component excess

Excessive concentration

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