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Exchange potential composition

To calculate thermal averages of A r) - Bix) we introduce a local exchange potential, A/r, that couples to the local composition, a - b [29] ... [Pg.11]

Instead of propagating the composition in time, we can study the time evolution of the exchange potential W. In equilibrium the density variable (pA - field variable W = i A - i B are related to each other via time evolution of the field W to the time dependence of the composition. Since the composition is a conserved quantity and it is linearly related to the field variable, we also expect the field W with which we are now describing our system to be conserved. Therefore, we can use the free energy functional M[W] from Eq. 42 and describe the dynamics of the field W through the relaxational dynamics of a model B system, referring to the classification introduced by Hohenberg and Halperin [94]. [Pg.40]

These main objectives can be reached only by modifying the structures and compositions of primarily the anode (methanol electrode) and secondarily the cathode (oxygen electrode) as discussed in Sections 111 and IV, respectively. In addition. Section IV discusses the conception of new proton exchange membranes with lower methanol permeability in order to improve the cathode characteristics. Section V deals with the progress in the development of DMFCs, while in Section VI the authors attempt to make a prognosis on the status of DMFC R D and its potential applications. [Pg.73]

Selectivity is one of the most important characteristics of an electrode, as it often determines whether a reliable measurement in the sample is possible or not. In practice, most pH sensitive membranes will also respond slightly to some interfering ions. As can be seen in Eq. (5), the potential of such a membrane is governed mainly by the activity of the hydrogen ion and also by the concentration of other interfering ions. To improve selectivity, advanced membrane compositions or protection membranes with size-exclusion or ion-exchange properties are often utilized. [Pg.292]

The SA-Tyrannohex has potential for use in heat exchangers due to its relatively high thermal conductivity at temperatures above 1000 °C. Figure 24 shows the thermal conductivity of the SA-Tyrannohex in the direction through the thickness and the fiber direction along with other materials including representative SiC/SiC composite (CVI). [Pg.137]

An obvious utility for the type of modeling described is to evaluate the effect of exchanging one material for another in a composite or an assembly or even the addition of a new material, perhaps one of high toxicity but with a low burning rate. It can be used to evaluate the contribution of a material that does not become involved until the later stages of a fire. The model has the potential of assessing the trade-offs of flammability vs. toxicity often encountered with the use of fire retardants. [Pg.18]

Where interactions between the (supercritical) gas and water are possible, there is rapid isotopic equilibration between the oxygen in C02 and H20. The potential to use this isotopic exchange equilibria as a measure of the extent of C02-water interaction, and thus as an indicator of C02 migration, is discussed in Kharaka etal. (2006). Unlike the results of Kharaka et al. (2006), there are no consistent changes in the oxygen isotopic composition of the fluid samples at the Otway site. [Pg.152]

This survey focuses on recent developments in catalysts for phosphoric acid fuel cells (PAFC), proton-exchange membrane fuel cells (PEMFC), and the direct methanol fuel cell (DMFC). In PAFC, operating at 160-220°C, orthophosphoric acid is used as the electrolyte, the anode catalyst is Pt and the cathode can be a bimetallic system like Pt/Cr/Co. For this purpose, a bimetallic colloidal precursor of the composition Pt50Co30Cr20 (size 3.8 nm) was prepared by the co-reduction of the corresponding metal salts [184-186], From XRD analysis, the bimetallic particles were found alloyed in an ordered fct-structure. The elecbocatalytic performance in a standard half-cell was compared with an industrial standard catalyst (bimetallic crystallites of 5.7 nm size) manufactured by co-precipitation and subsequent annealing to 900°C. The advantage of the bimetallic colloid catalysts lies in its improved durability, which is essential for PAFC applicabons. After 22 h it was found that the potential had decayed by less than 10 mV [187],... [Pg.84]

In principle, the three isotope method may be widely applied to new isotope systems such as Mg, Ca, Cr, Fe, Zn, Se, and Mo. Unlike isotopic analysis of purified oxygen, however, isotopic analysis of metals that have been separated from complex matrices commonly involves measurement of several isotopic ratios to monitor potential isobars, evaluate the internal consistency of the data through comparison with mass-dependent fractionation relations (e.g., Eqn. 8 above), or use in double-spike corrections for instrumental mass bias (Chapter 4 Albarede and Beard 2004). For experimental data that reflect partial isotopic exchange, their isotopic compositions will not lie along a mass-dependent fractionation line, but will instead lie along a line at high angle to a mass-dependent relation (Fig. 10), which will limit the use of multiple isotopic ratios for isobar corrections, data quality checks, and double-spike corrections. [Pg.17]


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See also in sourсe #XX -- [ Pg.243 ]




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