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Stages kinetics

The discovery development interface is important with respect to drug aqueous solubihty. In earlier discovery stages kinetic solubihty assays are perfectly acceptable even more desirable than the thermodynamic equilibrium solubihty assay. [Pg.275]

The computation of the curvatures from the bulk field differential geometry has proven to be rather imprecise. The errors produced by the use of the approximate formulas (100)-(104) are especially big if the spatial derivatives of the field sharp peaks at the phase interface. This is a common situation in the late-stage kinetics of the phase separating/ordering process, when the order parameter is saturated and the domains are separated by thin walls. Here, to calculate the curvatures, we propose a much more accurate method. It is based on the observation that the local curvatures are quantities that can be inferred solely from the shape of the interface, without appealing to the properties of the bulk field [Pg.212]

The role of Ca2+ in inducing refolding of a-lactalbumin is reflected in clean two-stage kinetics, with rate constants 6.0 and 1.3 s-1. The maximum concentration of the intermediate, monitored by stopped-flow fluorescence and time-resolved photo-CIDNP NMR, occurs at about 200 ms (327). [Pg.118]

Iron(III)-catalyzed autoxidation of ascorbic acid has received considerably less attention than the comparable reactions with copper species. Anaerobic studies confirmed that Fe(III) can easily oxidize ascorbic acid to dehydroascorbic acid. Xu and Jordan reported two-stage kinetics for this system in the presence of an excess of the metal ion, and suggested the fast formation of iron(III) ascorbate complexes which undergo reversible electron transfer steps (21). However, Bansch and coworkers did not find spectral evidence for the formation of ascorbate complexes in excess ascorbic acid (22). On the basis of a combined pH, temperature and pressure dependence study these authors confirmed that the oxidation by Fe(H20)g+ proceeds via an outer-sphere mechanism, while the reaction with Fe(H20)50H2+ is substitution-controlled and follows an inner-sphere electron transfer path. To some extent, these results may contradict with the model proposed by Taqui Khan and Martell (6), because the oxidation by the metal ion may take place before the ternary oxygen complex is actually formed in Eq. (17). [Pg.408]

Figure 15 Overall reaction rate and its approximations step 2 is rate-limiting. Dots represent the exact reaction rate dependence, solid line is the first-term hypergeometric approximation, dashed line corresponds to the reaction-rate equation that assumes the limitation of step 2 and dash-dots represent the equilibrium approximation. Hypergeometric approximation survives the 100-times increase in rate-limiting stage kinetic parameters and it works when there is no rate-limiting step at all. Parameters r, = 5, fj = 15, rj = 10 t2 = 0.2, fj = 0-1 (a) rj = 2,fj = - (b) t2 = 20, = 10, (c). Figure 15 Overall reaction rate and its approximations step 2 is rate-limiting. Dots represent the exact reaction rate dependence, solid line is the first-term hypergeometric approximation, dashed line corresponds to the reaction-rate equation that assumes the limitation of step 2 and dash-dots represent the equilibrium approximation. Hypergeometric approximation survives the 100-times increase in rate-limiting stage kinetic parameters and it works when there is no rate-limiting step at all. Parameters r, = 5, fj = 15, rj = 10 t2 = 0.2, fj = 0-1 (a) rj = 2,fj = - (b) t2 = 20, = 10, (c).
I Burner fuel stabilized with an oil-soluble petroleum sulfonate (Witco Petronate CR) in 1% NaCI was studied. Table 1 lists the variables and their ranges for the single-stage kinetic studies. A detailed description of the equipment, materials, and procedures has been presented by Byeseda.8... [Pg.215]

Karickhoff (1980) and Karickhoff et al. (1979) have studied sorption and desorption kinetics of hydrophobic pollutants on sediments. Sorption kinetics of pyrene, phenanthrene, and naphthalene on sediments showed an initial rapid increase in sorption with time (5-15 min) followed by a slow approach to equilibrium (Fig. 6.7). This same type of behavior was observed for pesticide sorption on soils and soil constituents and suggests rapid sorption on readily available sites followed by tortuous diffusion-controlled reactions. Karickhoff et al. (1979) modeled sorption of the hydrophobic aromatic hydrocarbons on the sediments using a two-stage kinetic process. The chemicals were fractionated into a labile state (equilibrium occurring in 1 h) and a nonlabile state. [Pg.143]

Since the introduction of a mathematical model for sintering by Kuczynski [12] numerous other models have been proposed. Reviews of these sintering kinetic models are given in references [13—19]. This description of sintering kinetics is organized into initial, intermediate, and final stage kinetic models. [Pg.788]

These experiments often display two-stage kinetic processes of which the second may be associated with irreversible binding (Karickhoff 1984 Pav-liostathis and Mathavan 1992). Some important details and the implication of slow desorption are given below. [Pg.148]

Table 7-5. Two-Stage Kinetics of Reduction of Germanium, Silicon, and Titanium from Their Tetrachlorides... Table 7-5. Two-Stage Kinetics of Reduction of Germanium, Silicon, and Titanium from Their Tetrachlorides...
Saiyasombati, P. and Kasting, G.B. (2003). Two-stage kinetic analysis of fragrance evaporation and absorption from skin, Interttational Journal of Cosmetic Science, 25, 235-243. [Pg.156]

Thus, let us denote the general features of PI, PPQ and SPPQ thermo-oxidation. The first important likeness of the degradation behaviour is O2 absorption at rather low temperatures (200 °C). At temperatures 250 °C or higher, when it becomes possible to search O2 absorption kinetics in real time, polymers display equal oxidation types independently of temperature - the three-stage kinetics, sequentially described by laws of the first and the zero orders with future autoacceleration. [Pg.188]

Figure 6. The sketch of the protein folding pathways. The fast (upper) folding pathway includes the formation of native-like collapsed states In, which rapidly convert into the native state N. The fraction of protein molecules, folding along this pathway, is >. For two-state folders, 1. The lower track (followed by 1 - molecules) represents slow pathway(s), which fold by a three-stage kinetic mechanism. At the first stage, nonspecific collapse species Insc form, which later convert into a collection of discrete native-like intermediates . The transition from Ij to the native state is slow and represents the rate-limiting step in the slow pathway. The degree of heterogeneity in the folding pathways depends on the sequence and external conditions. Figure 6. The sketch of the protein folding pathways. The fast (upper) folding pathway includes the formation of native-like collapsed states In, which rapidly convert into the native state N. The fraction of protein molecules, folding along this pathway, is >. For two-state folders, 1. The lower track (followed by 1 - molecules) represents slow pathway(s), which fold by a three-stage kinetic mechanism. At the first stage, nonspecific collapse species Insc form, which later convert into a collection of discrete native-like intermediates . The transition from Ij to the native state is slow and represents the rate-limiting step in the slow pathway. The degree of heterogeneity in the folding pathways depends on the sequence and external conditions.

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See also in sourсe #XX -- [ Pg.36 ]




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Adsorption kinetics model stages

Dissolution kinetics stages

Four-Stage Oxide-Bond-Forming Kinetics

Initial stage sintering kinetics

Intermediate stage sintering kinetics

Kinetic stages

Kinetic stages

Kinetics final stage

Kinetics initial stage

Kinetics intermediate stage

Kinetics of Emulsion Polymerization in Stage II, Case

Reversible many-stage reactions, kinetics

Sintering Kinetics by Stage

Surface kinetic reaction stages

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