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Elementary reaction rate

The Arrhenius relation given above for Are temperature dependence of air elementary reaction rate is used to find Are activation energy, E, aird Are pre-exponential factor. A, from the slope aird intercept, respectively, of a (linear) plot of n(l((T)) against 7 The stairdard enAralpv aird entropy chairges of Are trairsition state (at constairt... [Pg.2967]

In this study, the absorption rates of carbon dioxide into the solution of GMA and Aliquat 336 in such organic solvents as toluene, N-methyl-2-pirrolidinone(NMP), and dimethyl sulfoxide(DMSO) was measured to determine the pseudo-first-order reaction constant, which was used to obtain the elementary reaction rate constants. [Pg.345]

The overall reaction between CO2 and GMA was assumed to consist of two elementary reactions such as a reversible reaction of GMA and catalyst to form an intermediate and an irreversible reaction of this intermediate and carbon dioxide to form five-membered cyclic carbonate. Absorption data for CO2 in the solution at 101.3 N/m were interpreted to obtain pseudo-first-order reaction rate constant, which was used to obtain the elementary reaction rate constants. The effects of the solubility parameter of solvent on lc2/k and IC3 were explained using the solvent polarity. [Pg.348]

The single relaxation time approximation for all elementary reaction rates in a cycle with two limiting reactions is... [Pg.120]

Such a detailed description could in principle be made of every elementary step in a given reaction, while a dynamical simulation of a whole chemical process including several elementary steps is usually impossible. Typically intermediates in a reaction can have lifetimes which are many orders of magnitude larger than typical times for a dynamical simulation (a few picoseconds). Another point is that if the aim is to get an elementary reaction rate for a system at a given temperature, the full dynamical approach may be too detailed. [Pg.83]

It is impossible to understand all the complicated kinetic paths and to determine the elementary reaction rate constants without a detailed quantitative investigation of all the donor-acceptor interactions in the reaction system. Strictly speaking, at present there are no data on the elementary reaction rate constants even in low-molecular model systems. [Pg.120]

This type of reaction for which the rate equation can be written according to the stoichiometry is called an elementary reaction. Rate equations for such cases can easily be derived. Many reactions, however, are non-elementary, and consist of a series of elementary reactions. In such cases, we must assume all possible combinations of elementary reactions in order to determine one mechanism that is consistent with the experimental kinetic data. Usually, we can measure only the concentrations ofthe initial reactants and final products, since measurements of the concentrations of intermediate reactions in series are difficult. Thus, rate equations can be derived under assumptions that rates of change in the concentrations of those intermediates are approximately zero (steady-state approximation). An example of such treatment applied to an enzymatic reaction is shown in Section 3.2.2. [Pg.28]

The task of developing or extending a chemical kinetic model is facilitated since much of the necessary information is readily available. Section 13.3.1 deals with sources of thermodynamic and reaction-specific data. Once an elementary reaction is well characterized (i.e., the rate constant and product channel are known with sufficient accuracy), this information can be used in all reaction mechanisms where the reaction may be important. Large amounts of reaction specific data are now available, and methods for estimating and measuring elementary reaction rates have improved considerably over recent decades. [Pg.565]

When introducing the concept of the elementary reaction rate, we treated it as a number of elementary acts per unit volume or per unit surface for a unit time. But as a rule, the elementary character of a reaction and the number of elementary acts cannot be tested experimentally. Therefore it is important to determine a rate of reaction step using the kinetic equation... [Pg.105]

Comparison of elementary reaction rates indicates reactions (k5) and (fc14) (Figure 5.8) as the most significant processes for intermediate CH20 and final H2 and C02 products synthesis under current experimental conditions. This is associated with H02 radical predominance in the reaction system with H02J / L OIlJ = 103 - 104. [Pg.176]

III 4.2 Chemical Actinometers in the Ultraviolet Region. 127 111—5 Determination of the Elementary Reaction Rates, 128... [Pg.149]

Other reactions may be taken into consideration, with an effect on polymer structure, namely the formation of short- and long-chain branches. A complete list of reactions in S-PVC polymerization may be found in Kiparissides et al. [5]. On the above basis kinetic equations may be written. To keep it simple the chain transfer, back-biting and inhibition reactions are disregarded, while termination is considered to occur only by disproportionation. The elementary reaction rates for initiator decomposition and free radicals generation are as follows ... [Pg.372]

Kinetics and Mechanism of the Thermal DeNOx Reaction The discovery of the Thermal DeNOx reaction was followed by studies of its mechanism by the author and his coworkers and by other research groups. The former efforts culminated in the development of a kinetic data base and of a computer model2. The data base consisted of 742 data points distributed over a range of temperatures, reaction times, and initial concentrations of NO, NH3, 02, H2 and H2 O. The computer model used a set of 31 elementary reaction rates. Of these 31 reactions 27 had rate constants which were accurately known or could reasonably be estimated because they had little effect on the model s predictions. By using the remaining 4 reaction rate constants as adjustable parameters it was possible to fit the data base with its 7% experimental uncertainty. [Pg.3]

A majority of our experiments employed DMS-d as the sulfide reactant because more information concerning elementary reaction rates could be obtained in this matter (this aspect of our study is not discussed in detail in this paper). However, enough experiments were carried out with DMS to demonstrate that, within experimental uncertainty, kQ s values for OH reactions with DMS and DMS-d differ only by the difference in the abstraction rates. The pressure dependence data in air at 298K strongly supports this approximation. Substituting the appropriate Arrhenius parameters into equation 4 leads to the following expression for the temperature dependence of kQv for tlle 0H + DMS reaction 760 Torr air (units are cm ... [Pg.138]

Implicit to our considerations are a number of assumptions regarding the molecular details of the individual elementary reaction steps. The analysis of the kinetics presented here employed a simplified molecular reaction scheme. Our approach aimed at formulating explicit relationships between those elementary reaction rate constants that determine selectivity. [Pg.173]

Brune et have described a new tandem axis laser magnetic resonance (LMR), resonance fluorescence, and resonance absorption fast-flow apparatus for the study of the kinetics of elementary gas reactions. They placed emphasis on the simultaneous time-resolved detection of reactants and products, crosscalibration of detection axes, the use of multiple sources of free radicals and computer simulation of the time-dependence of the reactant and product concentrations in experiments designed to determine elementary reaction rate constants. They provided data for the reactions N + OH — H+NO, N-1-H02— products, O+OH— -H+02, and 0 + H02- OH+O2. [Pg.125]

The combustion of hydrocarbons covers an exceedingly wide temperature range (600-2500 K), so it is essential that kinetic data of many elementary reactions be obtained over a similar range. Elementary reaction rate... [Pg.565]

Adsorption and Elementary Reaction Rates Special attention has been given for a long time to the specific activities of catalysts as correlated with their adsorption characteristics. Nevertheless, no complete theory has been developed regarding these relationships. We shall here briefly discuss the relationship between adsorption and the elementary reaction rates, with reference to the work of Horiuti (11). [Pg.111]

Actual elementary reaction rates tend to follow the V H) or F(L) straight lines at higher or lower temperatures but deviate from these lines... [Pg.112]

Fig. 19. Temperature dependence of an heterogeneous elementary reaction rate. Reproduced from Horiuti (11). Fig. 19. Temperature dependence of an heterogeneous elementary reaction rate. Reproduced from Horiuti (11).
Schwab has pointed out that the following relationship between the two parameters of the Arrhenius equation is frequently encountered. A decrease in the activation energy of a given reaction, for a series of catalysts, often does not increase the reaction rate to the extent calculated, because of a simultaneous decrease of the frequency factor. Cremer (106) confirmed this for the decomposition of ethyl chloride on various chloride catalysts. These findings will be discussed here with due regard to the relation between adsorption and elementary reaction rates dealt with in the preceding section. [Pg.113]

Theoretical understanding of slow elementary chemical reactions is a central problem in chemical dynamics. A fundamental quantitative molecular picture of elementary reaction rates in aqueous solutions and at interfaces has proved extremely difficult to construct because of the role of the solvent, that is, the variety of physical and chemical effects resulting from interactions between reactants and solvent water molecules. The presence of ions at significant concentrations, extensive hydration of most species, and participation of water molecules in reactions as catalyst, intermediate, reactant, or product all serve to complicate mechanistic interpretation of slow aqueous reactions. Nonetheless, useful qualitative and quantitative interpretation is possible through considering known effects of hydration on thermodynamic properties. [Pg.71]

How well does this simple theory agree with experiment. By fitting data for gas-phase elementary reaction rates to the Arrhenius form, we can obtain the activation energy and the factor A. The value of A can be compared with the theory, once we estimate the molecular diameter. For the elementary reaction... [Pg.774]

Assuming power law (elementary reaction rate) kinetics to apply, write the rate equation for the following reactions ... [Pg.171]

The termination reactions shown are bimolecular these may occur either by recombination to give one chain, or, depending on the monomer, disproportionation to give two polymer chains (where DP is half that for recombination). The elementary reaction rate is... [Pg.63]

Process Elementary reaction Rate coefficient Rate of reaction... [Pg.64]

Table 1.11. Elementary reactions, rate coefficients and reaction rates for a simple cationic polymerization... Table 1.11. Elementary reactions, rate coefficients and reaction rates for a simple cationic polymerization...

See other pages where Elementary reaction rate is mentioned: [Pg.669]    [Pg.677]    [Pg.113]    [Pg.298]    [Pg.135]    [Pg.247]    [Pg.115]    [Pg.288]    [Pg.547]    [Pg.189]    [Pg.400]    [Pg.420]    [Pg.16]    [Pg.443]    [Pg.299]    [Pg.67]    [Pg.60]    [Pg.62]   
See also in sourсe #XX -- [ Pg.111 , Pg.112 ]




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