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Reaction rates of elementary reactions

These theories may have been covered (or at least mentioned) in your physical chemistry courses in statistical mechanics or kinetic theory of gases, but (mercifully) we will not go through them here because they involve a rather complex notation and are not necessary to describe chemical reactors. If you need reaction rate data very badly for some process, you will probably want to fmd the assistance of a chemist or physicist in calculating reaction rates of elementary reaction steps in order to formulate an accurate description of processes. [Pg.194]

The derivation above considered a two-step sequence on biographically nonuniform surfaces and followed the treatment first developed by Temkin. For induced nonuniform surfaces the reaction rates of elementary reactions are described by eq. 3.103-3.105. These general equations which take into account all the possible lateral interactions between all the surface adsorbed species on the surface can be applied to treat the same two-step sequence. [Pg.240]

The model description of the measured differences in high pressure oxidation is not satisfactory concerning the influence of small wato amounts. Eiiher the model is not complete or th e is a specific solvent effect in addition to the pressure effect on the chemical kinetics. Until now the reaction rate of elementary reactions at high pressure has been measured only in helium [e.g. 32] Calculation of the fugacity coefficients of the HO2 free radical in supCTcritical water also shows specific solvent interactions as a consequence of partial charges [33]. It can be assumed that these inta actions are much lower in supCTcritical carbon dioxide which may lead to somewhat different reaction rates of elementary reactions in the reaction network. [Pg.448]

Electrochemical impedance spectroscopy (EIS) is widely used for characterizing electrochemical systems. By measuring the impedance as a function of frequency, EIS provides a powerful tool for analyzing the performance losses in batteries and fuel cells. For example, Adler et al. have used EIS to identify the causes of fuel cell inefficiencies over a range of experimental operating conditions. KMC simulations can be used to better interpret experimental EIS observations and trace their atomic origins. Diffusion coefficients, electrode resistance, and reaction rates of elementary reactions can be identified with KMC simulations under various applied frequencies, and this information can be used to clarify the connections between EIS peaks or frequencies and the underlying reaction mechanisms. [Pg.189]

Wigner E 1937 Calculation of the rate of elementary associated reactions J. Chem. Phys. 5 720... [Pg.896]

In earlier chapters, we have seen how kinetic phenomena can be interpreted, for example, to provide a reaction scheme consisting of a set of elementary reactions. Over the years, several models have been devised to explain and sometimes to predict the rates of elementary reactions. It is these that we now wish to examine on a more fundamental basis in this chapter, plus Chapters 9 and 10. [Pg.155]

In microkinetics, overall rate expressions are deduced from the rates of elementary rate constants within a molecular mechanistic scheme of the reaction. We will use the methanation reaction as an example to illustrate the... [Pg.7]

This is the simplest of the models where violation of the Flory principle is permitted. The assumption behind this model stipulates that the reactivity of a polymer radical is predetermined by the type of bothjts ultimate and penultimate units [23]. Here, the pairs of terminal units MaM act, along with monomers M, as kinetically independent elements, so that there are m3 constants of the rate of elementary reactions of chain propagation ka ]r The stochastic process of conventional movement along macromolecules formed at fixed x will be Markovian, provided that monomeric units are differentiated by the type of preceding unit. In this case the number of transient states Sa of the extended Markov chain is m2 in accordance with the number of pairs of monomeric units. No special problems presents writing down the elements of the matrix of the transitions Q of such a chain [ 1,10,34,39] and deriving by means of the mathematical apparatus of the Markov chains the expressions for the instantaneous statistical characteristics of copolymers. By way of illustration this matrix will be presented for the case of binary copolymerization ... [Pg.180]

Presently, the effective role of reducible materials is strongly debated due to the fact that the reaction mechanisms earlier proposed involve steps both on the support and on the metal. Alternately, the nature of the metal-support may strongly modify the adsorptive properties of noble metals further altering the relative rates of elementary steps taking place over noble metal particles. [Pg.314]

Presently, the quantitative theory of irreversible polymeranalogous reactions proceeding in a kinetically-controlled regime is well along in development [ 16,17]. Particularly simple results are achieved in the framework of the ideal model, the only kinetic parameter of which is constant k of the rate of elementary reaction A + Z -> B. In this model the sequence distribution in macromolecules will be just the same as that in a random copolymer with parameters P(Mi ) = X =p and P(M2) = X2 = 1 - p where p is the conversion of functional group A that exponentially depends on time t and initial concen-... [Pg.149]

This region is determined by proportions between the rates of elementary reactions. For instance, when RH oxidation is chain-like and chains are terminated by the reaction R02 of with InH (mechanism III), the following six inequalities must be satisfied. [Pg.504]

Definitions for the variables and constants appearing in eqns. 1 and 2 are given in the nomenclature section at the end of this paper. The first of these equations represents a mass balance around the reactor, assuming that it operates in a differential manner. The second equation is a species balance written for the catalyst surface. The rate of elementary reaction j is represented by rj, and v j is the stoichiometric coefficient for component i in reaction j. The relationship of rj to the reactant partial pressures and surface species coverages are given by expressions of the form... [Pg.121]

This chapter presents the underlying fundamentals of the rates of elementary chemical reaction steps. In doing so, we outline the essential concepts and results from physical chemistry necessary to provide a basic understanding of how reactions occur. These concepts are then used to generate expressions for the rates of elementary reaction steps. The following chapters use these building blocks to develop intrinsic rate laws for a variety of chemical systems. Rather complicated, nonseparable rate laws for the overall reaction can result, or simple ones as in equation 6.1-1 or -2. [Pg.117]

Having chosen a particular model for the electrical properties of the interface, e.g., the TIM, it is necessary to incorporate the same model into the kinetic analysis. Just as electrical double layer (EDL) properties influence equilibrium partitioning between solid and liquid phases, they can also be expected to affect the rates of elementary reaction steps. An illustration of the effect of the EDL on adsorption/desorption reaction steps is shown schematically in Figure 7. In the case of lead ion adsorption onto a positively charged surface, the rate of adsorption is diminished and the rate of desorption enhanced relative to the case where there are no EDL effects. [Pg.125]

The application of helium permits the freezing of the reaction in such stages that the otherwise very reactive intermediates become detectable. Hydrogen thus influences the relative rates of elementary steps but not the overall meehanism which is shown in Fig. 4a (21,62). [Pg.284]

An accurate knowledge of the thermochemical properties of species, i.e., AHf(To), S Tq), and c T), is essential for the development of detailed chemical kinetic models. For example, the determination of heat release and removal rates by chemical reaction and the resulting changes in temperature in the mixture requires an accurate knowledge of AH and Cp for each species. In addition, reverse rates of elementary reactions are frequently determined by the application of the principle of microscopic reversibility, i.e., through the use of equilibrium constants, Clearly, to determine the knowledge of AH[ and S for all the species appearing in the reaction mechanism would be necessary. [Pg.111]

In spite of hundreds of papers and patents devoted to the polymerization of lactones only recently the first data on the rates of elementary reactions became available [1,2]. [Pg.271]

Chemical kinetics is the study of the rate at which chemical reactions proceed. Unless special care is taken, the measured rate of disappearance of some species may be due to the net contribution of several (elementary) reactions taking place. Thus we make a distinction between observed chemical rate expressions, discussed next, and rates of elementary reactions, treated subsequently. [Pg.381]

The direct determination of the rates of elementary photofragmentation reactions. These studies have provided information concerning the... [Pg.890]

Direct Determination of Rates of Elementary Photofragmentation Reactions. These studies have provided information concerning the molecular features that determine, for example, how energy is distributed among the products of a reaction, and they provide hints concerning when it is possible to achieve mode-selective dynamics in large molecules. [Pg.894]

The rates of elementary reactions may then be written in terms of the concentration of species involved and the rate constants, as follows. The rate of initiation is... [Pg.356]

If a system that is in equilibrium with respect to all stages of a complex reaction is being shifted to states more and more distant from equilibrium by gradual variation of concentrations of substances participating in the reaction, then, since the rates of elementary reactions may differ to any... [Pg.223]

The rate of elementary reactions of certain transition-metal complexes, such as insertions or substitutions, can be controlled by the substituents at the metal center. In favorable cases, usually in families of closely related systems, these substituents can affect the reactivities and the chemical shifts of the transition metal nuclei in a similar, parallel fashion, resulting in an apparent correlation of both properties. Modem DFT methods can reproduce these findings, provided that changes in rate constants are reflected in corresponding trends in activation barriers or BDEs on the potential energy surface. [Pg.248]

Generally speaking, s can be tended to zero by various methods without assuming S, bs, and bg to be constant. In this case, many different asymptotes arise. Their difference is associated with the fact that, at given 9 and cg, the values of w are independent of bs and be and the equations for "slow motions [the first part of eqn. (148)] contain parameters 1/S and bg/S. For example, at fixed bg, S and V, bs can be tended to zero ba -> 0. Then the rates of elementary reactions which are linear with respect to intermediates, will have an order of smallness e. But if the reaction also involves the participation of k intermediates as initial reactants, the order of smallness for w is equal to ek. Let kmin be the lowest order with respect to intermediates that can... [Pg.156]

On the basis of the principle of independency of the rates of elementary acts of chemical reactions, equations (2.5i)-(2.62) are assumed to be independent of each other. Therefore, the increases of layer thicknesses can explicitly be expressed from these equations as follows ... [Pg.79]

A more detailed form for writing the equation for parameter 8y can be based on the activated complex theory. The said theory predicts the following dependence for the rate of elementary chemical reaction i j ... [Pg.22]

This statement on the relationship between the stationary rate of the stepwise process and the thermodynamic force that initiates it can be easily generahzed for the case of an arbitrary combination of monomolecular transformations of intermediates. The simplest and most visual way to do that is to use the perfect analogy between equation (1.31) of the rate of elementary chemical reaction Vy and the Ohm s law for electric current ly between two points, i and j, of an electric circuit with electric potentials Ui and Uj, respectively ... [Pg.28]

An example is the stationary state of an open chemically reactive system, where the intermediate concentrations, which are setded in the course of the internal processes, are time constant. The rate of changing these interme diate concentrations (fluxes of these parameters) equals zero. Evidendy, the stationary state is setded at a certain ratio of the rates of elementary reactions responsible for the formation and vanishing of the reactive intermediates. [Pg.100]

Computational catalysis can make substantial contributions to these issues because it allows for a comparison of the rates of elementary reaction steps proposed for various mechanistic reaction paths. By use of computations, it is also possible to relate surface structure with the relative stabilities of various reaction intermediates and transition states. [Pg.130]

There are a number of possible approaches to the calculation of influences of finite-rate chemistry on diffusion flames. Known rates of elementary reaction steps may be employed in the full set of conservation equations, with solutions sought by numerical integration (for example, [171]). Complexities of diffusion-flame problems cause this approach to be difficult to pursue and motivate searches for simplifications of the chemical kinetics [172]. Numerical integrations that have been performed mainly employ one-step (first in [107]) or two-step [173] approximations to the kinetics. Appropriate one-step approximations are realistic for limited purposes over restricted ranges of conditions. However, there are important aspects of flame structure (for example, soot-concentration profiles) that cannot be described by one-step, overall, kinetic schemes, and one of the major currently outstanding diffusion-flame problems is to develop better simplified kinetic models for hydrocarbon diffusion flames that are capable of predicting results such as observed correlations [172] for concentration profiles of nonequilibrium species. [Pg.72]

The remainder of this chapter describes methods to determine the rate and temperature dependence of the rate of elementary reactions. This information is used to describe how reaction rates in general are appraised. [Pg.54]


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