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Chemical kinetics reaction order

TRANSIENT CHEMICAL SPECIES REACTION MECHANISM CHEMICAL KINETICS Reaction order of nonenzymic reaction, CHEMICAL KINETICS NOYES EQUATION... [Pg.777]

In chemical kinetics, reaction orders are the most important parameters in determining reaction mechanisms. Reaction orders were first introduced into electrode kinetics by Vetter (64). For determination of reaction orders, double layer effects are suppressed by working in excess of supporting electrolyte and rates are compared at constant electrode potential V (i.e., constant potential drop across the metal-solution interface) as a function of concentration. Then,... [Pg.389]

An entire mechanism can be unimolecular, provided that the rate-limiting step is unimolecular. See also Chemical Kinetics, Molecularity Order of Reaction Elementary Reactions... [Pg.694]

CHEMICAL KINETICS First-order rate behavior, AUTOPHOSPHORYLATION FIRST-ORDER REACTION KINETICS ORDER OF REACTION HALF-LIFE... [Pg.743]

ORDER OF REACTION MOLECULARITY CHEMICAL KINETICS FIRST-ORDER REACTIONS RATE CONSTANTS... [Pg.767]

NONEQUILIBRIUM THERMODYNAMICS A PRIMER UNIMOLECULAR CHEMICAL KINETICS MOLECULARITY ORDER OF REACTION ELEMENTARY REACTIONS Unimolecular forward/bimolecular reverse, CHEMICAL KINETICS Unimolecular isomerization,... [Pg.786]

In all CVD processes, we are dealing with the change from one state (i.e., the initial, low-temperature reactant gases) to a later one (i.e., the final state with some solid phase and product gases) in time. Since any practical commercial process must be completed quickly, the rate with which one proceeds from the initial to the final state is important. This rate will depend on chemical kinetics (reaction rates) and fluid dynamic transport phenomena. Therefore, in order to clearly understand CVD processes, we will not only examine chemical thermodynamics (Section 1.2), but also kinetics and transport (Section 1.3). [Pg.1]

Gedanken Flame Experiment. In order to illustrate how the problems caused by the requirements of temporal and spatial resolution and geometric and physical complexity are translated into computational cost, we have chosen to analyze a gedanken flame experiment. Consider a closed tube one meter long which contains a combustible gas mixture. We wish to calculate how the physical properties such as temperature, species densities, and position of the flame front change after the mixture is ignited at one end. The burning gas can be described, we assume, by a chemical kinetics reaction rate scheme which involves some tens of species and hundreds of chemical reactions, some of which are "stiff."... [Pg.336]

But, without the reaction rate R, we can go no further. We must either find the rate from experiment or, perhaps, predict the rate from a theory of reaction rates. We must turn to the discipline of chemical kinetics in order to find d ldt. [Pg.60]

The order of a reaction and molecularity must be included in discussing chemical kinetics. The order of a reaction is determined from the mathematical expression showing the dependence of rate on the concentration of the reactants, and the molecularity by the number of molecules invdljved in the reaction. [Pg.766]

When the kinetic reaction order is one, a binary chemical reaction forms a mixed dipole (capacitive-conductive) in the physical chemical energy variety. When the order of the kinetic reaction is different from one, a binary reaction still forms a dipole, but in another variety of energy, the chemical reaction energy. [Pg.157]

The number of ions which can cross the boundary per unit time, and thus the exchange rate and exchange current density, are determined by the laws of chemical kinetics. In order to say more about this exchange rate we must consider the energetic situation of the ion in question at the surface of the electrode phase. There it will preferentially be in an energy minimum which lies no higher than that of the solvated ion otherwise the reverse reaction ... [Pg.19]

In this section we review the application of kinetics to several simple chemical reactions, focusing on how the integrated form of the rate law can be used to determine reaction orders. In addition, we consider how rate laws for more complex systems can be determined. [Pg.751]

Among the earlier studies of reaction kinetics in mechanically stirred slurry reactors may be noted the papers of Davis et al. (D3), Price and Schiewitz (P5), and Littman and Bliss (L6). The latter investigated the hydrogenation of toluene catalyzed by Raney-nickel with a view to establishing the mechanism of the reaction and reaction orders, the study being a typical example of the application of mechanically stirred reactors for investigations of chemical kinetics in the absence of mass-transfer effects. [Pg.123]

According to the definition given, this is a second-order reaction. Clearly, however, it is not bimolecular, illustrating that there is distinction between the order of a reaction and its molecularity. The former refers to exponents in the rate equation the latter, to the number of solute species in an elementary reaction. The order of a reaction is determined by kinetic experiments, which will be detailed in the chapters that follow. The term molecularity refers to a chemical reaction step, and it does not follow simply and unambiguously from the reaction order. In fact, the methods by which the mechanism (one feature of which is the molecularity of the participating reaction steps) is determined will be presented in Chapter 6 these steps are not always either simple or unambiguous. It is not very useful to try to define a molecularity for reaction (1-13), although the molecularity of the several individual steps of which it is comprised can be defined. [Pg.6]

The units on [CH3CeH4S02H] are inverse molarity. Reciprocal concentrations are often cited in the chemical kinetics literature for second-order reactions. Confirm that second-order kinetics provide a good fit and determine the rate constant. [Pg.251]

Many, if not most, of the key reactions of chemistry are second-order reactions, and understanding this type of reaction is central to understanding chemical kinetics. Cellular automata models of second-order reactions are therefore very important they can illustrate the salient features of these reactions and greatly aid in this understanding. [Pg.126]

Integrals involving partial fractions occur often in chemical kinetics. For example, the differential equation which represents a second-order reaction is... [Pg.239]

Fractional and Other Order Reactions in Constant Volume Systems. In chemical kinetics, one frequently encounters reactions whose orders are not integers. Consider a reaction involving only a single reactant A whose rate expression is of the form... [Pg.31]

In general an analysis of a system in which noncompetitive parallel reactions are taking place is considerably more difficult than analyses of the type discussed in Chapter 3. In dealing with parallel reactions one must deal with the problems of determining reaction orders and rate constants for each of the individual reactions. The chemical engineer must be careful both in planning the experiment and in analyzing the data so as to obtain values of the kinetic con-... [Pg.146]

Recall that we are assuming faem "C faff (°r fax, if turbulent flow). Anyone who has carefully observed a laminar diffusion flame - preferably one with little soot, e.g. burning a small amount of alcohol, say, in a whiskey glass of Sambucca - can perceive of a thin flame (sheet) of blue incandescence from CH radicals or some yellow from heated soot in the reaction zone. As in the premixed flame (laminar deflagration), this flame is of the order of 1 mm in thickness. A quenched candle flame produced by the insertion of a metal screen would also reveal this thin yellow (soot) luminous cup-shaped sheet of flame. Although wind or turbulence would distort and convolute this flame sheet, locally its structure would be preserved provided that faem fax. As a consequence of the fast chemical kinetics time, we can idealize the flame sheet as an infinitessimal sheet. The reaction then occurs at y = yf in our one dimensional model. [Pg.244]

The global rates of heat generation and gas evolution must be known quite accurately for inherently safe design.. These rates depend on reaction kinetics, which are functions of variables such as temperature, reactant concentrations, reaction order, addition rates, catalyst concentrations, and mass transfer. The kinetics are often determined at different scales, e.g., during product development in laboratory tests in combination with chemical analysis or during pilot plant trials. These tests provide relevant information regarding requirements... [Pg.93]

First law of thermodynamics, 24 645-648 First limiting amino acid, 2 601 First-order irreversible chemical kinetics, 25 286-287, 292-293 First-principle approach, in particle size measurement, 13 153 First sale doctrine, 7 793 Fischer, Emil, 16 768 Fischer carbene reaction, 24 35-36 Fischer esterification, 10 499 Fischer formula, 4 697 Fischer-Indole synthesis, 9 288 Fischer lock and key hypothesis, 24 38 Fischer-Tropsch (FT) synthesis, 6 791, 827 12 431... [Pg.361]

In chemical equilibria, the energy relations between the reactants and the products are governed by thermodynamics without concerning the intermediate states or time. In chemical kinetics, the time variable is introduced and rate of change of concentration of reactants or products with respect to time is followed. The chemical kinetics is thus, concerned with the quantitative determination of rate of chemical reactions and of the factors upon which the rates depend. With the knowledge of effect of various factors, such as concentration, pressure, temperature, medium, effect of catalyst etc., on reaction rate, one can consider an interpretation of the empirical laws in terms of reaction mechanism. Let us first define the terms such as rate, rate constant, order, molecularity etc. before going into detail. [Pg.1]

Another example from chemical kinetics can be seen in the rate equation for first-order reactions. Here the equation relating the concentration of a species A at time t, [A](/), to the reaction time and the initial concentration, [A](0), is... [Pg.7]


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See also in sourсe #XX -- [ Pg.28 , Pg.36 ]




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