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Ideal reference system

At first sight, there seems to be a basic difference between the two regimes with respect to the influence of Kia/Vl. In the water-phase-controlled regime, the overall exchange velocity, via/w, is independent of Kia/v/, whereas in the air-phase controlled regime v(a/w is linearly related to Ga/w. Yet, this asymmetry is just a consequence of our decision to relate all concentrations to the water phase. In fact, for substances with small Kia/v/ values, the aqueous phase is not the ideal reference system to describe air-water exchange. This can be best demonstrated for the case of exchange of water itself (Kia/V1 = 2.3 x 10 5 at 25°C), that is, for the evaporation of water. [Pg.894]

We bear in mind however that the values of p (T,p) and y, depend upon the choice of the ideal reference system. If we choose for the solvent a reference system in which y, becomes unity as xt approaches unity, the unitary chemical potential p (T,p) is given by the chemical potential p (T,p) of the pure solvent i ut(T,p) = p (T,p). On the other hand, if we choose for the solute substances a reference system in which y, becomes unity as xt approaches zero, the unitary chemical potential ju (r,p) is given by the chemical potential p (T,p) of the solute i at infinite dilution p ( T,p) = p (T,p). [Pg.72]

The surface excess amount, or Gibbs adsorption (see Section 6.2.3), of a component i, that is, /if, is defined as the excess of the quantity of this component actually present in the system, in excess of that present in an ideal reference system of the same volume as the real system, and in which the bulk concentrations in the two phases stay uniform up to the GDS. Nevertheless, the discussion of this topic is difficult on the other hand for the purposes of this book, it is enough to describe the practical methodology, in which the amount of solute adsorbed from the liquid phase is calculated by subtracting the remaining concentration after adsorption from the concentration at the beginning of the adsorption process. [Pg.310]

The introduction of the activity and activity coefficients enables a comparison to he made quite simply between the properties of a given system and those of the ideal reference system. [Pg.89]

If we compare this with (7.52) we see that the standard chemical potential is the same as before, but the chemical potential of mixing is altered the activity ai—Xiyi replaces the mole fraction Xi, This may be generalized to other thermodynamic quantities. The standard properties of a non-ideal system are the same as those of the corresponding ideal reference system. It is only the quantities dependent upon composition that are altered by the introduction of activity coefficients. This is illustrated by table 7.2 which is to be compared with table 7.1. [Pg.90]

Here then we have a non-ideal system (c/. chap. VII, 8) which may be compared with an ideal reference system consisting of a gas mixture of the same composition, and at the same temperature T but at a pressure sufficiently low that the mixture behaves as a perfect mixture. [Pg.154]

It is important to note that the spin-statistical factor is obtained here without having to rely on a theoretical value for fedif- The values provide an empirical measure of fcutf in ideal reference system, since diffussion coefficients and encounter distances must cancel in the ratio. [Pg.13]

These considerations lead to a relation between the rate constant A in a nonideal system and the rate constant Ao in the corresponding ideal reference system ... [Pg.54]

The first self-consistent PRISM studies by Schweizer et al. considered only the HNC-style solvation potential and were based on an optimized perturbative, not variational, determination of the ideal reference system effective bending energy. The starting point is a simple functional expansion of the true single-chain free energy about an ideal reference system" ... [Pg.110]

Let us give a brief summary of the LSGF method. We will consider a system of N atoms somehow distributed on the underlying primitive lattice. We start with the notion that if we choose an unperturbed reference system which has an ideal periodicity by placing eciuivalent effective scatterers on the same underlying lattice, its Hamiltonian may be calculated in the reciprocal space. Corresponding unperturbed Green s... [Pg.115]

The reliability of the results depends in large measure on how well deviations from the (ideal) linear relationship between log / and dry weight per unit area can be eliminated or allowed for. As is well known, this can be accomplished by the comparative method (3.10), provided that standard (reference system) and unknown, identical in mass, shape, and elementary composition, are exposed to the same x-ray beam. In the cytological investigations, these conditions are difficult to meet, not only because the samples are complex in composition, but also because they are very small, as is clear from the units employed (micromicrograms per square micron or 10 12 gram per 10 8 sq cm). [Pg.297]

Reference electrodes for non-aqueous solvents are always troublesome because the necessary salt bridge may add considerable errors by undefined junction potentials. Leakage of components of the reference compartment, water in particular, into the working electrode compartment is a further problem. Whenever electrochemical cells of very small dimensions have to be designed, the construction of a suitable reference electrode system may be very difficult. Thus, an ideal reference electrode would be a simple wire introduced into the test cell. The usefulness of redox modified electrodes as reference electrodes in this respect has been studied in some detail... [Pg.80]

The endpoint measurement of the ideal test system must be objective, so that a given compound will give similar results when tested using the standard test protocol in different laboratories. If it is not possible to obtain reproductive results in a given laboratory over time or between various laboratories, then the historical database against which new compounds are evaluated will be time- and laboratory-dependent. Along these lines, it is important for the test protocol to incorporate internal standards to serve as quality controls. Thus, test data could be represented utilizing a reference scale based on the test system response to the internal controls. Such normalization, if properly documented, could reduce intertest variability. [Pg.642]

Here G°(T) refers to an n mole ideal gas system at a standard pressure designated as P° (usually 1 bar). The chemical potential of a one component i ideal gas system is then... [Pg.85]

It is well known that insertion of the above effective coefficients Se and Pe or De = Pe/Se into Eqs. (2) or (3) respectively, does not lead to the correct description of transient diffusion. However, the behaviour of the ideal Fickian system defined by Se and Pe or De constitutes a useful standard of reference. Given the appropriate theoretical background, one may then deduce information about S(X), DT(X) from the nature and magnitude of the deviation of suitable observed kinetic parameters from the calculated Fickian values. [Pg.131]

One further consideration as to the choice of a reference system in competition kinetic studies should be mentioned. That is, in cases where the competitor substance, here both MSA and DMS02, react at substantially lower rates than the reference system, the presence of even small amounts of impurities in the system which could react at a faster rate with OH could bias the analysis. Ideally, the reference system rate and that of the substrate being measured should be similar in magnitude. [Pg.526]

With the example of an HF plant, Ponton aimed at developing guidelines for inexpensive plant construction. The idea of using reactors of limited lifetime and made of disposable and recyclable materials, referred to as disposable batch plant [58, 60], was oriented on the highly sophisticated chemical manufacture of living organisms, animals and plants. Ideally, such systems would require no internal cleaning, repair or maintenance. [Pg.523]

In general a necessary part of a potentiometric measurement is the coupling of a reference electrode to the indicating electrode. The ideal reference electrode has a number of important characteristics (1) a reproducible potential, (2) a low-temperature coefficient, (3) the capacity to remain unpolarized when small currents are drawn, and (4) inertness to the sample solution. If the reference electrode must be prepared in the laboratory, a convenient and reproducible system is desirable. [Pg.35]

Although all potentiometric measurements (except those involving membrane electrodes) ultimately are based on a redox couple, the method can be applied to oxidation-reduction processes, acid-base processes, precipitation processes, and metal ion complexation processes. Measurements that involve a component of a redox couple require that either the oxidized or reduced conjugate of the species to be measured be maintained at a constant and known activity at the electrode. If the goal is to measure the activity of silver ion in a solution, then a silver wire coupled to the appropriate reference electrodes makes an ideal potentiometric system. Likewise, if the goal is to monitor iron(UI) concentrations with a platinum electrode, a known concentration of... [Pg.38]

We first take as a reference system an infinitely dilute solution of solute 2 in solvent 1. The chemical potentials of solvent 1 and solute 2, then, are given in the form of Eq. 8.13 for an ideal solution and in the form of Eq. 8.14 for a non-ideal solution ... [Pg.75]

The symmetrical reference system is based on Raoult s law in a perfect solution, while the unsymmetrical reference system is based on Henry s law in an ideal dilute solution. [Pg.75]

In this section we shall always define the activity coefficients with respect to the symmetrical reference system. Comparing Eq. 8.7 and Eq. 8.17, we define the excess free enthalpy (excess Gibbs energy) gE per mole of a non-ideal binary solution as Eq. 8.18 ... [Pg.76]

This excess enthalpy hE corresponds to the heat of mixing of the non-ideal binary solution at constant pressure. Namely, hE = xf + x2h with - ht -h - -RT2(dlny JdT), where hf is the partial molar heat of mixing of substance i, ht is the partial molar enthalpy of i in the non-ideal binary solution, and h° is the molar enthalpy of pure substance i. Remind ourselves that the reference system for the activity coefficients is symmetrical. [Pg.76]

A discrepancy in free enthalpy between the perfect solution and the non-ideal solution, if the reference system is symmetrical, is generally expressed by the excess free enthalpy GE, which consists of the enthalpy term HE and the entropy term -TSE i.e. GE = HE - TSE. Two situations arise accordingly in non-ideal solutions depending on which of the two terms, He and - TSE, is dominant The non-ideal solution is called regular, if its deviation from the perfect solution is caused mostly by the excess enthalpy (heat of mixing) HE ... [Pg.77]


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See also in sourсe #XX -- [ Pg.88 ]




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