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Molarity volume of solution and

In the event that the molar volumes of solute and solvent are not comparable, and the thermal agitation is not adequate to achieve maximum entropy of mixing, a nonideal entropy of mixing exists (Bustamante et al., 1989). Two equations that account for the nonideal entropy of mixing have been derived by considering the partial molal volurfiA,and the volume fraction, occupied by each solution component. The L rst was developed by Flory and Huggins (Hildebrand, 1949 Kertes, 1965) ... [Pg.6]

Tc, numbers of adsorbent sites occupied by the solute and solvent, respectively, and V and van der Waals molar volumes of solute and solvent, respectively Kf is the ratio of the equilibrium concentrations of the solute in the stationary and mobile phases at infinite dilution of the solute ... [Pg.108]

Solution For every entry of the table in the previous example we calculate the molar volume of solution and the corresponding mol fraction of ethanol. The calculation is facilitated by choosing a basis of 1 kg of solution. The moles of each component are... [Pg.413]

Molar volumes of solute and solvent, Vy and Vs, are determined from apparent molar volumes Oy (Section II.F) by density measurements. In terms of the measured densities of the solution and the pure solvent, d and d, the apparent molar volume is given by (molarity and molality scale, respectively)... [Pg.96]

Sample Problem 4.9 illustrates how to use these equations to solve for molarity, volume of solution, and moles of solute. [Pg.136]

A stock solution is prepared by weighing out an appropriate portion of a pure solid or by measuring out an appropriate volume of a pure liquid and diluting to a known volume. Exactly how this is done depends on the required concentration units. For example, to prepare a solution with a desired molarity you would weigh out an appropriate mass of the reagent, dissolve it in a portion of solvent, and bring to the desired volume. To prepare a solution where the solute s concentration is given as a volume percent, you would measure out an appropriate volume of solute and add sufficient solvent to obtain the desired total volume. [Pg.30]

P rtl IMol r Properties. The properties of individual components in a mixture or solution play an important role in solution thermodynamics. These properties, which represent molar derivatives of such extensive quantities as Gibbs free energy and entropy, are called partial molar properties. For example, in a Hquid mixture of ethanol and water, the partial molar volume of ethanol and the partial molar volume of water have values that are, in general, quite different from the volumes of pure ethanol and pure water at the same temperature and pressure (21). If the mixture is an ideal solution, the partial molar volume of a component in solution is the same as the molar volume of the pure material at the same temperature and pressure. [Pg.235]

Calculate the molarity of a solute in a solution, volume of solution, and mass of solute, given the other two quantities (Examples G.1-G.3). [Pg.83]

The effect of pressure on chemical equilibria and rates of reactions can be described by the well-known equations resulting from the pressure dependence of the Gibbs enthalpy of reaction and activation, respectively, shown in Scheme 1. The volume of reaction (AV) corresponds to the difference between the partial molar volumes of reactants and products. Within the scope of transition state theory the volume of activation can be, accordingly, considered to be a measure of the partial molar volume of the transition state (TS) with respect to the partial molar volumes of the reactants. Volumes of reaction can be determined in three ways (a) from the pressure dependence of the equilibrium constant (from the plot of In K vs p) (b) from the measurement of partial molar volumes of all reactants and products derived from the densities, d, of the solution of each individual component measured at various concentrations, c, and extrapolation of the apparent molar volume 4>... [Pg.548]

Figure 3.1 Mixing of nA moles of A and wg moles of B at constant p and T. The molar volumes of pure A and B are Fa and Fg. The partial molar volumes of A and B in the solution are VA and FB, respectively. Figure 3.1 Mixing of nA moles of A and wg moles of B at constant p and T. The molar volumes of pure A and B are Fa and Fg. The partial molar volumes of A and B in the solution are VA and FB, respectively.
A particularly simple case is shown in Figure 18.1, in which the volume is a linear function of the mole number of glycolamide in a kilogram of water. In this case, the partial molar volume of solute is constant and is equal to the slope of the line. The partial molar volume represents the effective volume of the solute in solution, that is, the increase in volume per mole of solute added. From Equation (9.27), written for the volume function. [Pg.408]

In Fiery s theory of the excluded volume (27), the chains in undiluted polymer systems assume their unperturbed dimensions. The expansion factor in solutions is governed by the parameter (J — x)/v, v being the molar volume of solvent and x the segment-solvent interaction (regular solution) parameter. In undiluted polymers, the solvent for any molecule is simply other polymer molecules. If it is assumed that the excluded volume term in the thermodynamic theory of concentrated systems can be applied directly to the determination of coil dimensions, then x is automatically zero but v is very large, reducing the expansion to zero. [Pg.8]

Fig. 29a-c. Effects of three parameters of the equation of states in the text, (a) With increasing a, the transition temperature decreases when p and the molar volume of solute are equal to zero, (b) with decreasing P, discontinuity increases when a and the molar volume of solute are equal to zero, and (c) with increasing v the swelling ratio decreases and the transition temperature slightly increases when a and p are equal to zero. [Pg.236]

This volume is called partial molar volume of A and denoted by symbol. V A. This partial volume is dependent on the composition of the solution. If the composition changes, this value also changes. As T, P and nB are kept constant during the process, we may define file partial molar volume as... [Pg.75]

Here, E, is the current utilization, / is the membrane permselectivity, T is the transport number, n is the number of cell pairs in the stack, Vw is the partial molar volume of water, and C is the concentration, a, c, s and w refer to anion, cation, solution and water, respectively, and the superscripts cm, am, c, and d refer to cation-exchange membrane, anion-exchange membrane, concentrate and diluate. [Pg.100]

The measurement of partial molar quantities will be illustrated with reference to partial molar volumes. We can measure absolute volumes of solution and, thus, can determine partial molar volumes directly from its definition ... [Pg.230]

Strictly speaking, this holds only for both the solution and pure component under the vapor pressure of component i. However, because the molar volumes of solutions are small, the result is little changed at other pressures. [Pg.232]

Fig. 8.1 Volume per mole as a function of the molar fraction x2 of solute 2 in a binary perfect solution and in an ideal dilute solution v2 = the unitary partial molar volume of solute 2 extrapolated to x2 — 1. Fig. 8.1 Volume per mole as a function of the molar fraction x2 of solute 2 in a binary perfect solution and in an ideal dilute solution v2 = the unitary partial molar volume of solute 2 extrapolated to x2 — 1.
For the calculation of the net adsorption enthalpies of transactinides on metal surfaces the partial molar enthalpies of solution and the enthalpy of displacement are required. These values can be obtained using the semi-empirical Miedema model [66-70] and the Volume-Vacancy or Surface-Vacancy model [32,70,71]. Data for these calculations are given in [34,72,73]. [Pg.231]


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See also in sourсe #XX -- [ Pg.546 ]




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Molarity of solutions

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Volume of solutions

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