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McKay equation

This result, the McKay equation, is often written in terms of F, the fraction of exchange, as... [Pg.57]

A plot to analyze kinetic data for the exchange of benzyl iodide and iodide ions in ethanol at 27.3 °C. The line shows that log 1 - F) decreases linearly with time according to the McKay equation, Eq. (3-56). The data are given in Table 3-3. [Pg.58]

Im and Busch, using the optical activity method, have also made a study of the exchange of the propylenediaminetetraacetate complexes of Co(III) and Co(II) (CoPY and CoPY ). This system can be treated by the McKay equation. Optical rotation data was obtained at temperatures between 80 and 100°C and various pH s between 2.0 and 7.0. This was again found to be consistent with exchange via two pathways k and k )... [Pg.118]

The pseudo first-order rate constants, obs, are obtained by least-squares fits of the measured peak height increase of the relevant coalesced oxygen-17 signal as a function of time to the modified McKay equation (7, 67, 68). The kinetics can be studied by manipulation of... [Pg.91]

Fig. 16. Slow isotopic exchange at 35.0°C on Re(V) center, (a) Oxygen-17 spectra showing signal growth vs time for [Re02(CN)4]3. (b) Least-squares fit of the data to the modified exponential McKay equation (7). The total complex concentration [Re] = 0.2 m, pH = 6.6, and fi = 1.2 m (KN03). (Adapted with permission from Roodt, A. Leipoldt, J. G. Helm, L. Abou-Hamdan, A. Merbach, A. E. Inorg. Chem. 1995, 34, 560-568. Copyright 1995 American Chemical Society.)... Fig. 16. Slow isotopic exchange at 35.0°C on Re(V) center, (a) Oxygen-17 spectra showing signal growth vs time for [Re02(CN)4]3. (b) Least-squares fit of the data to the modified exponential McKay equation (7). The total complex concentration [Re] = 0.2 m, pH = 6.6, and fi = 1.2 m (KN03). (Adapted with permission from Roodt, A. Leipoldt, J. G. Helm, L. Abou-Hamdan, A. Merbach, A. E. Inorg. Chem. 1995, 34, 560-568. Copyright 1995 American Chemical Society.)...
As in the case of the oxygen exchange described above in Section IV (see also Fig. 16), well-behaved first-order kinetics were observed for all the cyanide exchange reactions for which the modified exponential form of the McKay equation (8) was used to determine the observed rate constants. [Pg.101]

The upper part of Table 3-3 gives the results of one experiment. The semilogarith-mic plot based on the McKay expression is displayed in Fig. 3-5. From it, the half-time of exchange is 1410 s. Equation (3-57) then gives Rex = 2.10 X 10 6 mol L-1 s l. [Pg.57]

McKay (2) showed the possibility of using the Euler cross differentiation equation for the thermodynamic treatment of a three-component system. [Pg.364]

McKay [44, 45] proved that the homogeneous reaction for such systems invariably proceeds according to the first-order equation... [Pg.81]

In the past, much attention was given to the study of dye and iodine adsorption by active carbons (Bmnauer, 1945 Orr and Dalla Valle, 1959). Many studies have been made with dye molecules of well-known size, shape and chemical properties, but the results have not been easy to interpret (Giles et al., 1970 McKay, 1982, 1984). In a systematic study of iodine adsorption (from aqueous solution) on a carbon black and four activated carbons (Femandez-Colinas etal., 1989b), it was found that the iodine isotherms could be analysed by the as-method. In this way it was possible to assess values of the available volume in pores of effective width of 0.5-1.5 nm. The adsorption of iodine was also featured in a recent study by Ziolkowska and Garbacz (1997), who applied the Langmuir, Freundlich and other isotherm equations. [Pg.280]

Formalism According to Pitzer. The most common method for the evaluation of the activity and osmotic coefficients of an electrolyte in a binary mixture of strong electrolytes with a common ion is by Scatchard s Equations (23), the McKay-Perring treatment (24), Mayers Equations... [Pg.271]

Figure 12 The apparent 1 bar free energy of fusion of hypothetical REEMgAlSi06 clinopyroxene plotted as a function of temperature. Experimental data for all REE and Y were used and D values were corrected to. Results were fitted to Equation (24). Key Gallahan and Nielsen (1992), Watson et al. (1987), Blundy (unpublished data), X Hart and Dunn (1993), O Hack et al (1994), Grutzeck et al (1974), Gaetani and Grove (1995), O Hauri et al (1994), A Dunn (1986), Jones and Burnett (1987), McKay et al (1986), + McKay et al (1994), A Nicholls... Figure 12 The apparent 1 bar free energy of fusion of hypothetical REEMgAlSi06 clinopyroxene plotted as a function of temperature. Experimental data for all REE and Y were used and D values were corrected to. Results were fitted to Equation (24). Key Gallahan and Nielsen (1992), Watson et al. (1987), Blundy (unpublished data), X Hart and Dunn (1993), O Hack et al (1994), Grutzeck et al (1974), Gaetani and Grove (1995), O Hauri et al (1994), A Dunn (1986), Jones and Burnett (1987), McKay et al (1986), + McKay et al (1994), A Nicholls...
In the case of MZ twins, the correlation, B, between phenotypes G) and G2 is 1 while for DZ twins the correlation if 0.5. Therefore, data on twins provides us with a pair of simultaneous equations, which by substitution and rearrangement, gives a straightforward formula for / 2 (Falconer McKay 1996)... [Pg.246]

To understand better the sorption process of dyes of various types of anion exchange resins, it is essential to determine the course of this process in time and the effect of different factors affecting their retention. The rate at which the dissolved dye is removed horn the aqueous solution by solid sorbents is a significant factor for application in wastewater quality control, too. It is essential to evaluate the adsorption kinetics using theoretical models in order to design and control the sorption process units. Two common kinetic models, namely, the Lagergren pseudo first-order model (Equation 4) and the Ho and McKay pseudo second-order model (Equation 5) were fitted to the experimental data of dyes sorption on the anion exchangers ... [Pg.63]

In order to minimize contact time, it is necessary to use a contact time model, which may be a kinetic model (first order, second order, Elovich kinetics, etc.) or a mass transport diffusion model (film, pore, surface, pore-surface). The present case study is based on a pseudo-second order kinetic model (Ho and McKay, 1998), and the kinetic equation is ... [Pg.350]

The differential form of the pseudo-first-order kinetic model could be expressed by the following equation (Ho and McKay, 1998 Igwe and Abia, 2007)... [Pg.17]

As in the nematic liquid crystal case, it is clear that (6,78) represents a balance of forces at equilibrium. This can be seen by applying arguments that parallel those in Remark (i) on page 40. Similarly, it can be shown that the equilibrium equations (6.79) and (6.80) actually arise from a balance of moments, as has been demonstrated by Stewart and McKay [267], by means of an appropriate extension to the Ericksen identity (B.6) (cf. [181]). For the present, however, we restrict our attention to the derivation of the couple stress tensor Uj and its associated couple stress vector Analogous to the discussion for the nematic case in Remark (i) on page 40 when the balance of moments was discussed, consider an arbitrary, infinitesimal, rigid body rotation a for which... [Pg.264]


See other pages where McKay equation is mentioned: [Pg.57]    [Pg.256]    [Pg.54]    [Pg.360]    [Pg.364]    [Pg.255]    [Pg.1781]    [Pg.57]    [Pg.256]    [Pg.54]    [Pg.360]    [Pg.364]    [Pg.255]    [Pg.1781]    [Pg.235]    [Pg.28]    [Pg.235]    [Pg.585]    [Pg.202]    [Pg.88]    [Pg.10]    [Pg.489]    [Pg.65]    [Pg.65]    [Pg.48]    [Pg.420]    [Pg.361]    [Pg.91]    [Pg.91]    [Pg.268]    [Pg.339]   
See also in sourсe #XX -- [ Pg.57 , Pg.69 , Pg.118 ]

See also in sourсe #XX -- [ Pg.360 ]

See also in sourсe #XX -- [ Pg.1781 ]




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