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Kinetic analysis formulation

Langmuir s research on how oxygen gas deteriorated the tungsten filaments of light bulbs led to a theory of adsorption that relates the surface concentration of a gas to its pressure above the surface (1915). This, together with Taylor s concept of active sites on the surface of a catalyst, enabled Hinshelwood in around 1927 to formulate the Langmuir-Hinshelwood kinetics that we still use today to describe catalytic reactions. Indeed, research in catalysis was synonymous with kinetic analysis... [Pg.23]

Kinetic information on the chemical changes of excipient compatibility samples is a direct outcome of most formulation compatibility studies. Because accelerated conditions of thermal and thermal humidity stress are employed, degradation will often occur at these conditions. A brief kinetic evaluation of the data can address the behavior and extent of decay such that degradation data can effectively be utilized to determine levels and conditions of compatibility (96). It is not the aim of this section to recommend full kinetic treatment of decay rather it is to describe simple concepts and exercises that will help the excipient compatibility formulator utilize their data most effectively. Several experimental factors can be included in the initial experimental design of excipient compatibility studies to make kinetic analysis more powerful, and even with small studies having a limited amount of samples for analysis, a brief kinetic treatment of the data is recommended. [Pg.446]

Various types of possible interactions between reactions are discussed. Some of them are united by the general idea of chemical reaction interference. The ideas on conjugated reactions are broadened and the determinant formula is deduced the coherence condition for chemical interference is formulated and associated phase shifts are determined. It is shown how interaction between reactions may be qualitatively and quantitatively assessed and kinetic analysis of complex reactions with under-researched mechanisms may be performed with simultaneous consideration of the stationary concentration method. Using particular examples, interference of hydrogen peroxide dissociation and oxidation of substrates is considered. [Pg.19]

The desire to formulate reaction schemes in terms of molecular processes taking place on a catalyst surface must be balanced with the need to express the reaction scheme in terms of kinetic parameters that are accessible to experimental measurement or theoretical prediction. This compromise between mechanistic detail and kinetic parameter estimation plays an important role in the use of reaction kinetics analysis to describe the reaction chemistry for a catalytic process. Here, we discuss four case studies in which different compromises are made to develop an adequate kinetic model that describes the available observations determined experimentally and/or theoretically. For convenience, we selected these examples from our work in this field however, this selection is arbitrary, and many other examples could have been chosen from the literature. [Pg.189]

A simplified reaction scheme for the kinetic analysis of radical chain halogenations can be formulated as follows ... [Pg.27]

In 2003, Cenini and coworkers reported (tetraarylporphyrin)cobalt(II) complexes 326 as efficient catalysts (1 mol%) for cyclopropanations. In the absence of air, styrenes 321 underwent an efficient cyclopropanation with ethyl diazoacetate 322 giving cyclopropanes 324 in 65-99% yield with 3-5 1 trans/cis ratios (Fig. 77) [348]. Simple olefins and more hindered diazoesters did not react. With diazoacetate and hydrocarbons, such as cyclohexane or benzene, C-H insertion took place furnishing cyclohexyl- or phenylacetate. In line with Ikeno s proposal the cyclopropanation reaction was considerably slowed down in the presence of TEMPO, though not completely inhibited. Based on a kinetic analysis a two-electron catalytic cycle with a bridged carbene unit was formulated, however. [Pg.277]

The construction of a kinetic model for an animal cell culture involves several steps a kinetic analysis of the experimental results with the formulation of hypotheses on the nature of the rate-limiting steps the choice of rate expressions describing the influence of these phenomena on the cellular processes evaluation of parameter values and validation of the model with different experimental results. In this section a general methodology is described for the modelling of cell cultures, and the procedure is illustrated on the kinetics of a hybridoma cell. (For a summary of terms used, see Table 4.3.3.)... [Pg.160]

The demonstration that yield-time data for a particular rate process are satisfactorily represented by a rate equation from the set in Table 3.3. is a usefiil initial result (as in all kinetic analyses), but formulation of a reaction model requires more support than a statistical comparison with the fit of the same data to other rate equations. Some important aspects of kinetic analysis are summarized below. [Pg.110]

Thus, the question of central concern raised in our contribution has been the macroscopic formulation of EET and its relation to the experimental observable of excimer fluorescence in a time-resolved experiment. EET has been discussed, hers, as a dispersive, i.e., time-depen-dent process in deterministic monomer-excimer models which had been the subject of a detailed kinetic analysis in recent work (3 8, 4.S.). With the use of rate function k(t) (Equation 4) it is natural to yield typical non-exponential intensity-time profiles, either in form of an asymptotic approach (Equations 5,6), or in closed form analytical solutions (Equations 7,8). The physios emer-... [Pg.236]

Our discussion up to this point has dealt with the use of kinetics to describe the rates of chemically well-defined reactions and to explore the mechanism of reactions. Kinetic formulations can be used in what one might call the opposite sense—that is, to provide an empirical mathematical framework in which data from complex reactions can be analyzed. The objective here is a simplification of complex situations, not the discovery of exact mechanism from kinetic analysis. Two examples of this use of kinetic formulations that are relevant to aquatic systems will be given here. The first concerns treatment of data from the biochemic ... [Pg.48]

Recently, the activation and thermodynamic parameters for the catalytic DTBCH2 oxidation promoted by [Cu2(L55)]" in a mixed aqueous/organic, cryogenic solvent have been obtained (157). The catecholase reaction proceeds also in this case with a biphasic rate of DTBQ development, and the rates of the two steps still exhibit hyperbolic dependence on DTBCH2 concentration. However, the second step under these conditions also depends linearly on O2 concentration. The spectroscopic and kinetic analysis of the system allow the formulation of the following mechanism ... [Pg.218]

To a large extent, the formal kinetic analysis techniques presented in this chapter relate to discontinuous batch operations. Even if the goal is a continuous operation, the batch process kinetic model serves as a start-up. The most significant element of a kinetic analysis is the time dependence of the macroscopic process variables mentioned in Chap. 2. Bacteria, molds, viruses, and yeasts all have different reproduction mechanisms, and formulating a structured kinetic model more closely related to the actual mechanism is a desirable goal. More structured models are desirable not only to deal with active cells but also to extend kinetic analysis to more complex situations involving inactive cells, mixed populations of cells, multiple substrates, and... [Pg.197]

Pantani R, Speranza V, Titomanlio G (2001b) Relevance of (syrstallization kinetics in the simulation of injection molding process. Int Polym Process 16 61-71 Park SJ, Kwon TH (1996) Sensitivity analysis formulation for three-dimensional conduction heat transfer with complex geometries using a boundary element method. Int J Numer Methods Eng 39 2837-2862... [Pg.172]

Dehydroquinate synthetase, the enzyme responsible for the cyclisation of DAHP (9) to give 3-dehydroquinate (10), the first cyclic intermediate in the shikimate pathway, was obtmned in partially purified form from Escherichia coli. The enzyme required Co and NAD" " (but not NADP" ) for full activity. No intermediates were isolable when these cofactors were removed but it was observed in a kinetic analysis of the enzymic transformation that the release of orthophosphate, the disappearance of DAHP and the formation of 3-dehydroquinate aU proceeded at the same rate. These observations indicated, it was suggested, that one enzyme was responsible for the whole sequence of reactions necessary for the convosion. On the basis of these observations, Sprinson and his collaborators formulated a working hypothesis for the steps involved in the cyclisation of the substrate DAHP and this is discussed in more detail later. [Pg.11]

Many elements of a mathematical model of the catalytic converter are available in the classical chemical reactor engineering literature. There are also many novel features in the automotive catalytic converter that need further analysis or even new formulations the transient analysis of catalytic beds, the shallow pellet bed, the monolith and the stacked and rolled screens, the negative order kinetics of CO oxidation over platinum,... [Pg.114]


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Kinetic analysis

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