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The Kinetic Approach

The kinetic approach towards PAMs is carried out mostly and has been used for the synthesis of numerous shape-persistent macrocycles. This approach will be discussed first. The thermodynamic approach has only recently been used for the construction of PAMs and will be discussed afterwards. The intention of this chapter is not a full coverage of all reported synthetic procedures towards shape-persistent macrocycles with nanometer-scale interiors. Rather, typical examples will point up the different existing procedures, including their advantages and disadvantages. [Pg.227]

Nitrophenyl glycosides and glycosyl fluorides are particularly attractive donors in this regard, not only because of their generally high cat/ m values, but also because the departed aglycone is itself a very poor acceptor and thus will not compete as an acceptor. It is also very easily separated from the products. [Pg.728]

Although some disaccharides, e.g. lactose, can serve as very inexpensive donors, complications can arise if the glucose liberated itself acts as an acceptor. A more unusual donor that has been used is the sialyl lactoside of a water-soluble polymer, [Pg.728]

In a further example Crout demonstrated a major difference in product distribution when the A-acetylgalactosaminidase from Aspergillus oryzae transfers GalNAc to methyl aGalNAc or to methyl pGalNAc. Transfer to methyl a-galactoside resulted in 81% yield of the 1-4 linked product and only 9% of the 1-6 isomer whereas transfer to methyl P-galactoside resulted in almost equal amounts of the two isomers, but at lower yields (20% of the 1-4 isomer and 23% of the 1-6 isomer) [27]. [Pg.732]


If we define p and Pj. as the probability of addition occurring in the meso and racemic modes, respectively, then p Pr since there are only two possibilities. The probability p is the analog of Pjj for copolymers hence, by analogy with Eq. (7.30), this equals the fraction of isotactic dyads among all dyads. In terms of the kinetic approach of the last section, p is equal to the rate of an iso addition divided by the combined rates of iso and syndio additions ... [Pg.476]

Surface Area and Permeability or Porosity. Gas or solute adsorption is typicaUy used to evaluate surface area (74,75), and mercury porosimetry is used, ia coajuactioa with at least oae other particle-size analysis, eg, electron microscopy, to assess permeabUity (76). Experimental techniques and theoretical models have been developed to elucidate the nature and quantity of pores (74,77). These iaclude the kinetic approach to gas adsorptioa of Bmaauer, Emmett, and TeUer (78), known as the BET method and which is based on Langmuir s adsorption model (79), the potential theory of Polanyi (25,80) for gas adsorption, the experimental aspects of solute adsorption (25,81), and the principles of mercury porosimetry, based on the Young-Duprn expression (24,25). [Pg.395]

Enzymatic Catalysis. Enzymes are biological catalysts. They increase the rate of a chemical reaction without undergoing permanent change and without affecting the reaction equiUbrium. The thermodynamic approach to the study of a chemical reaction calculates the equiUbrium concentrations using the thermodynamic properties of the substrates and products. This approach gives no information about the rate at which the equiUbrium is reached. The kinetic approach is concerned with the reaction rates and the factors that determine these, eg, pH, temperature, and presence of a catalyst. Therefore, the kinetic approach is essentially an experimental investigation. [Pg.286]

Study of reversible reactions close to equilibrium. This possibility was discussed in eonnection with Scheme II and is further treated in Chapter 4. It turns out that if the displacement from equilibrium is small, the kinetics approach first-order behavior. [Pg.78]

Development of the theory of nucleation is the long-standing problem in the statistical physics. The kinetic approach to this problem was proposed by Zeldovich" . For the nucleation rate. 7. i.e. for the number of critical and supercritical embryos being formed in the unit volume per unit time at early stages of nucleation, he obtained the following expression... [Pg.111]

Mechanistically, in approximately neutral solutions, solid state diffusion is dominant. At higher or lower pH values, iron becomes increasingly soluble and the corrosion rate increases with the kinetics approaching linearity, ultimately being limited by the rate of diffusion of iron species through the pores in the oxide layer. In more concentrated solutions, e.g. pH values of less than 3 or greater than 12 (relative to 25°C) the oxide becomes detached from the metal and therefore unprotective . It may be noted that similar Arrhenius factors have been found at 75 C to those given by extrapolation of Potter and Mann s data from 300°C. [Pg.842]

Many reactions show appreciable reversibility. This section introduces thermodynamic methods for estimating equilibrium compositions from free energies of reaction, and relates these methods to the kinetic approach where the equilibrium composition is found by equating the forward and reverse reaction rates. [Pg.234]

Equilibrium Constants. We begin with the kinetic approach. Refer to Equations (1.14) and (1.15) and rewrite (1.15) as... [Pg.235]

There are three approaches that may be used in deriving mathematical expressions for an adsorption isotherm. The first utilizes kinetic expressions for the rates of adsorption and desorption. At equilibrium these two rates must be equal. A second approach involves the use of statistical thermodynamics to obtain a pseudo equilibrium constant for the process in terms of the partition functions of vacant sites, adsorbed molecules, and gas phase molecules. A third approach using classical thermodynamics is also possible. Because it provides a useful physical picture of the molecular processes involved, we will adopt the kinetic approach in our derivations. [Pg.173]

Derivation of the Langmuir Equation— Adsorption of a Single Species. The kinetic approach to deriving a mathematical expression for the Langmuir isotherm assumes that the rate of adsorption on the surface is proportional to the product of the partial pressure of the adsorbate in the gas phase and the fraction of the surface that is bare. (Adsorption may occur only when a gas phase molecule strikes an uncovered site.) If the fraction of the surface covered by an adsorbed gas A is denoted by 0Ay the fraction that is bare will be 1 — 0A if no other species are adsorbed. If the partial pressure of A in the gas phase is PA, the rate of adsorption is given by... [Pg.174]

In this case the kinetic approach to the derivation of the Langmuir equation requires that the process be regarded as a reaction between the gas molecule and Wo surface sites. Thus the... [Pg.176]

In the special case of an ideal single catalyst pore, we have to take into account that diffusion is quicker than in a porous particle, where the tortuous nature of the pores has to be considered. Hence, the tortuosity r has to be regarded. Furthermore, the mass-related surface area AmBEX is used to calculate the surface-related rate constant based on the experimentally determined mass-related rate constant. Finally, the gas phase concentrations of the kinetic approach (Equation 12.14) were replaced by the liquid phase concentrations via the Henry coefficient. This yields the following differential equation ... [Pg.220]

Each of these two experimental approaches are charaterized by respective advantages and disadvantages (1) in D-B-A systems, the kinetic approach measures the average rate of the one-electron transfer occurring in each D-B-A... [Pg.109]

Nevertheless, the kinetic approach to heterogeneous catalysis can be rewarding if relative data for two or more structurally related reactants or catalysts are acquired and interpreted. Instead of applying several assumptions that simplify the reaction scheme and the model of the surface, which are necessary for absolute kinetic description, it is accepted that, under certain conditions, the same reaction scheme holds for all members of the series of reactants or catalysts and that all of the unknown but identical simplifications in the relative data cancel out. However, it is much safer to select a series of reactants in which the structural change from one member to another will be small enough to uphold the basic features of the mechanism than to assume the same for a set of catalysts that are not minor variations of a basic preparation. [Pg.152]

We have seen how a comparison of the equilibrium constant estimated from kinetic data for the forward and reverse directions (i.e. K = kf/k ) with that obtained by measurements on the equilibrated system, may be used to provide strong support (or otherwise) for a particular reaction scheme (see also Chap. 8 Pd(II)). The kinetic approach may be useful also for providing information on thermodynamic data not otherwise easily available. [Pg.49]

Occasionally it is as useful to obtain relative constants for a series of reactants acting on a common substrate, as it is to have actual rate values. Relative rate constants are obtained by competition methods, which avoid the kinetic approach entirely. The method is well illustrated by considering the second-order reactions of two Co(III) complexes Co" and Cob" (which might, for example, be Co(NH3)5CP and Co(NH3)5Br +), with a common reductant (Cr(II) (leading in this case to CrCU and CrBr + respectively) ... [Pg.176]

The fundamentals of the kinetic approach to water-rock interaction are constituted by the quantitative assessment of reaction kinetics for mineral hydrolysis and precipitation. These may be expressed in terms of rates of change in molality... [Pg.587]

KINETIC CHARACTERIZATION OF TRANSPORTERS. Stein has provided a useful outline of kinetic approaches to characterize transport systems. In each of the approaches, the investigator must accurately determine the amount of substrate transported at a defined point of time after the substrate and the membrane system have contacted each other. The kinetic approaches include ... [Pg.449]

It is interesting to note that due to their industrial importance, free radical polymerizations are the most studied reactions in chemistry. Furthermore, the kinetic approaches taken in this chapter are experimentally verified for essentially all typical free radical vinyl polymerizations. [Pg.183]

In contrast to the kinetic approach, deviations from the terminal model have also been treated from a thermodynamic viewpoint [Kruger et al., 1987 Lowry, 1960 Palmer et al., 2000, 2001]. Altered copolymer compositions in certain copolymerizations are accounted for in this treatment in terms of the tendency of one of the monomers (M2) to depropagate. An essential difference between the kinetic and thermodynamic treatments is that the latter implies that the copolymer composition can vary with the concentrations of the monomers. If the concentration of monomer M2 falls below its equilibrium value [M]c at the particular reaction temperature, terminal M2 units will be prone to depropagate. The result would be a... [Pg.515]

There is another, nonkinetic parameter widely used when evaluating a heat sterilization process. This is the F0 value, defined as the number of minutes required to kill all endospores present in a system held at a temperature of 250°F or 121°C. It should be noted that, in principle, the kinetic approach implies that sterilization cannot be achieved (because there is no zero on a logarithmic plot) so the nonkinetic offers more hope. The F0 can be measured and there is an interconnection between F0 and D if F0 is slightly redefined as the number, n, of D values required to sterilize a system, i.e., F0 = nD. [Pg.185]

All these fracture pressures are large negative pressures, the liquid being under great tension. The values show that the kinetic approach can be used to predict limiting values for this condition. If a substance were... [Pg.49]

Nevertheless, the earlier thermodynamic treatment left one significant equation still very much present and effective when a change toward the kinetic approach occurred. This equation (Nemst s law) is used today and probably will be used even when all electrochemical calculations are wrapped up inside various companies software offerings. Nemst s equation,11 which treats the electrode/solution interface at equilibrium in a thermodynamic way, is the subject of the following section. [Pg.340]

It is quite natural that the thermodynamic approach does not allow photocorrosion processes to be described comprehensively. In a number of cases, kinetic peculiarities of reactions play an important role (see, for example, Bard and Wrighton, 1977) these peculiarities are caused by the effect of crystalline structure, state of the semiconductor surface, etc. A detailed description of a complicated reaction with several particles in the solution and crystal lattice involved usually encounters considerable difficulties. Therefore, at this stage the kinetic approach is used to reveal purely qualitative regularities of corrosion processes. [Pg.292]

Equation (23) obviously gives the two-dimensional ideal gas law when a > a2 and with the o2 term included represents part of the correction included in Equation (15). This model for surfaces is, of course, no more successful than the one-component gas model used in the kinetic approach however, it does call attention to the role of the substrate as part of the entire picture of monolayers. We saw in Chapter 3 that solution nonideality may also be considered in osmotic equilibrium. Pursuing this approach still further results in the concept of phase separation to form two immiscible surface solutions, which returns us to the phase transitions described above. [Pg.315]

Norbert Berkowitz I once again question the admissibility of the kinetic approach. Hydrogen yields at the various temperatures are not normalized, and that implies the quite untenable assumption that hydrogen yields at all experimental temperatures would all be the same provided sufficiently long degasification periods were allowed. I doubt whether the authors actually do imply that, but if they don t, they ought to bear in mind that classical kinetics... [Pg.612]

The said allows us to understand the importance of the kinetic approach developed for the first time by Waite and Leibfried [21, 22]. In essence, as is seen from Fig. 1.15 and Fig. 1.26, their approach to the simplest A + B —0 reaction does not differ from the Smoluchowski one However, coincidence of the two mathematical formalisms in this particular case does not mean that theories are basically identical. Indeed, the Waite-Leibfried equations are derived as some approximation of the exact kinetic equations due to a simplified treatment of the fluctuational spectrum a complete set of the joint correlation functions x(rJ) for kinds of particles is replaced by the only function xab (a t) describing the correlation of chemically reacting dissimilar particles. Second, the equation defining the correlation function X = Xab(aO is linearized in the function x(rJ)- This is analogous to the... [Pg.43]

Work is in progress in order to satisfactorily define the kinetic approach. [Pg.435]

The kinetic approach that has been most extensively applied to glutamine synthetase is that of equilibrium isotope exchange (85-88). Experimental procedures involve preparing a series of reaction solutions at chemical equilibrium and monitoring the following exchanges ... [Pg.351]


See other pages where The Kinetic Approach is mentioned: [Pg.9]    [Pg.21]    [Pg.179]    [Pg.191]    [Pg.248]    [Pg.248]    [Pg.33]    [Pg.85]    [Pg.110]    [Pg.257]    [Pg.128]    [Pg.391]    [Pg.277]    [Pg.218]    [Pg.517]    [Pg.1223]    [Pg.16]    [Pg.1223]    [Pg.50]    [Pg.603]    [Pg.178]    [Pg.372]   


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Kinetic approach

Kinetics approach

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