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Rate Laws A Summary

In the last several sections we have developed the following important points  [Pg.724]

To simplify the rate laws for reactions, vve have always assumed that the rate is being studied under conditions where only the forward reaction is important. This produces rate laws that contain only reactant concentrations. [Pg.724]

Whether we determine the differential rate law or the integrated rate law depends on the type of data that can be collected conveniently and accurately. Once we have experimentally determined either type of rate law for a given reaction, we can write the other rate law. [Pg.725]

The most common method for experimentally determining the differential rate law is the method of initial rates. In this method several experiments are run at different initial concentrations, and the instantaneous rates are determined for each at the same value of t as close to t = 0 as possible. The point is to evaluate the rate before the concentrations change significantly from the initial values. From a comparison of the initial rates and the initial concentrations, the dependence of the rate on the concentrations of various reactants can be obtained—that is, the order in each reactant can be determined. [Pg.725]

The integrated rate law for a reaction that involves several reactants can be treated by choosing conditions such that the concentration of only one [Pg.725]

Suppose we run this reaction under conditions where [BrOs Jo = 1.0 X 10 M, [Br ]o = 1.0 M, and [H ]o = 1.0 M. As the reaction proceeds, [Br03 ] decreases significantly, but because the Br ion and ion concentrations are so large initially, relatively httle of either of these two reactants is consnmed. Thus [Br ] and [H ] remain approximately constant. In other words, nnder the conditions where the Br ion and ion concentrations are mnch larger than the BrOs ion concentration, we can assnme that throughout the reaction [Pg.735]

Note that the kinetics of complicated reactions can be stndied by observing the behavior of one reactant at a time. If the concentration of one reactant is much smaller than the concentrations of the others, then the amounts of those reactants present in large concentrations will not change significantly and can be regarded as constant. The change in concentration with time of the reactant present in a relatively small amount can then be used to determine the order of the reaction in that component. This technique allows us to determine rate laws for complex reactions. [Pg.735]

Summary of the Kinetics for Reactions of the Type oA- Products That Are Zero, First, or Second [Pg.736]


In summary, when a reaction is said to be an elementary reaction, the reaction rate law has been experimentally investigated and found to follow the above rate law. One special case is single-step radioactive decay reactions, which are elementary reactions and do not require further experimental confirmation of the reaction rate law. For other reactions, no matter how simple the reaction may be, without experimental confirmation, one cannot say a priori that it is an elementary reaction and cannot write down the reaction rate law, as shown by the complicated reaction rate law of Reaction 1-34. On the other hand, if the reaction rate law of Reaction 1-36 is found to be Equation 1-37, Reaction 1-36 may or may not be an elementary reaction. For example, Reaction 1-32 is not an elementary reaction even though the simple reaction law is consistent with an elementary reaction (Bamford and Tipper, 1972, p. 206). [Pg.15]

For series a3 points have been limited to 20% reaction for any one solution for series al points have been limited to 10% reaction. Within these limits satisfactory linear relations are also obtained for these two series. Outside the specified limits for series a3 and al there was a tendency for points to lie above the lines represented. However, for some solutions of series a3 and for most solutions of series al, some turbidity developed after the reaction had progressed for some time. In summary, for solutions of series a5 the suggested rate law appears to hold through to the middle stages of reaction, while for solutions of series a3 and al it holds for the early stages of reaction. From Figure 5 it is fairly clear that the values of k n/kf and kn/kr are a function of the reaction medium. [Pg.240]

In summary, the parabolic rate law may be derived using eqn. (152) to determine the fluxes, with the adsorption layer composition determined by the equilibrium relationship (161) with [A](s) = [B](s) for a salt AB. Because the integration step is considered to be the rate-limiting process, it is of considerable interest to evaluate If the rate constant for the removal of water from the anion is much larger than for the cation, the dehydration of the cation will be rate-limiting. In this instance... [Pg.216]

In summary, the rate law for a reaction relates reaction rate, the rate constant k, and the concentration of the reactants. Although the equation for a reaction conveys a great deal of information, it is important to remember that the actual rate law and order of a complex reaction can be determined only by experiment. [Pg.545]

Table 2.2 is a summary of the differential and integrated forms of some simple rate laws. Also listed are expressions for the reaction half-times corresponding to several of the integrated rate expressions. These are the times at which the concentration of a reactant is half its initial value. [Pg.58]

Table 4-2 shows, as an example, a summary of the effects of experimental variables on the ion-exchange rate controlled by intraparticle diffusion, and by liquid-phase mass transfer. Further details and special situations will become apparent in the discussion of rate laws to follow. [Pg.107]

In summary, for many reactions involving multiple steps and pathways, the powers in the rate laws surprisingly agree with the stoichiometric coefficients. Consequently, to facilitate describing this class of reactions, we say a reaction/o//o>v.t an elementary rate law when the reaction orders are identical with the stoichiometric coefficients of the reacting species for the reaction as written. It is important to remember that the rate laws are determined by experimental observation They are a function of the reaction chemistry and not the type of reactor in which the reactions occur. Table 3-1 gives examples of rate laws for a number of reactions. [Pg.84]

The derivation of the rate law is given in the Summary Notes on the web and CD-RO.M. Equation (7-42) is in the form of the rate law that is given for an enzymatic reaction exhibiting noncompetitive inhibiiion. Heavy metal ions such as Pb" . Ag , and Hg ". as well a.s inhibitors that react with the enzy me lo form chemical derivatives, are typical examples of noncompetitive inhibitors. [Pg.414]

In this section and the previous two, we discussed a series of experimental and mathematical methods for the study of reaction kinetics. Figure 16.10 is a useful summary of this information. Note that the integrated rate law provides an alternative method for obtaining reaction orders and the rate constant. [Pg.517]

In reallity the chemical equation (1.4) does not tell us how reactants become products - it is a summary of the overall process. In fact it is molecularity, e.g. the number of species that must collide to produce the reaction which determines the form of a rate equation. Reactions whose rate law can be written from its molecularity are called elementary. The kinetics of the elementary step depends only on the number of reactant molecules in that step. [Pg.10]

According to the first law of thermodynamics, the energy (cal) in our consumed fuel can never be lost. Consumed fuel is either oxidized to meet the energy demands of the basal metabolic rate + exercise, or it is stored as fat. Thus, an intake of calories in excess of those expended results in weight gain. The simple statement, If you eat too much and don t exercise, you will get fat, is really a summary of the bioenergetics of the ATP-ADP cycle. [Pg.356]

In summary. Ho and Fishbein s paper verifies the mechanistic conclusions of their previous investigations on a broader basis In addition, it contains the first comparison of the decomposition kinetics of a pair of (Z)- and (F )-diazenolates. The isomeric 2,2,2-trifluoroethyldiazenolates were studied comparatively, i. e., under the same reaction conditions. Ho and Fishbein found that the (Z)-diazenolate follows the same rate law as the (F )-isomer, and that the (Z)-isomer reacts much faster in the acid-independent process (rate constant ki) and in the acid-catalyzed process ( h) i(Z)/ i( ) = 2600 and A h(Z)/ h( ) = HOOO, respectively. Broxton and Stray (1982) reported a roughly comparable ratio for methyl 4-nitrophenyldiazenolate ( 10 ). [Pg.250]

At present a number of equations of this type are known some of them have four parameters. They are used not only for structure-reactivity and structure-equilibrium correlations but also for description of effects of structure on spectral properties of organic molecules, and of effects of media on reaction rates. The Bronsted law for homogeneous catalysis was recognized also as a linear free energy relationship. A summary of all equations can be found in some of the recent reviews (2,3). [Pg.76]

In Table 3.4 is a summary of some eomparisons provided by Weller on the basis of this argument. The power-law correlations generally provide an adequate representation of the rate data, although they are not (nor do they propose to be) strongly based on any fundamental consideration of nonideal surfaces. In fact, the adequacy of both power-law and LH equations can be explained, in part, by the fact that the general LH form,... [Pg.195]

A summary of intraparticle transport criteria is given in Table 7.2. The most general of the criteria, 5(a) of Table 7.2, ensures the absence of any net effects (combined) of temperature and concentration gradients but does not guarantee that this may not be due to a compensation between heat- and mass-transport rates. (In fact, this is the case when y/f ). It may therefore be the most conservative general policy to see that the separate criteria for isothermality are met, for example, by the combination of 3 and 5(c), or of 3 and 4 in Table 7.2. The presentations of Table 7.2 deal with power-law kinetics only more complicated issues, such as what to do with complex kinetics or reactions involving volume change, have also been treated in the literature and are summarized by Mears [reference 5(b) in Table 7.2]. [Pg.494]

Hence, 0a = 1, by definition. In summary, aU partial pressures in the rate law should be written as a product of total pressure and mole fraction. Then, mole fractions can be expressed in terms of the conversion of CO. Alternatively, the ideal gas law can be used to express partial pressures p, as QRT, and the conversion dependence of molar density C, is tabulated by Fogler (1999, p. 96) for variable-volume gas-phase flow reactors. It should be emphasized that y, ptotai and CiRT generate the same function of conversion when the s parameter in Fogler s expressions is written as... [Pg.59]

The initial reactant product conversion rate should increase at higher temperature because kinetic rate constants for elementary steps, particularly the desorption of gas D, increase at higher temperature. In summary, there is no total pressure dependence of the initial reactant product conversion rate when (1) A -h B C -h D, (2) single-site adsorption is appropriate for each component, and (3) desorption of one of the products controls the Hougen-Watson kinetic rate law. [Pg.420]

The power law kinetic equation could be a simplified form of a mechanistic scheme. A summary of some of the reported reaction orders for the partial pressure of hydrogen and carbon monoxide which have been obtained from power law fits by different groups are listed in Table 9. The partial pressure dependencies vary rather widely. The power law fits were obtained for different cobalt catalysts prepared using different supports and methods. The data in Table 9 show that there is not one best power law equation that would provide a good fit for all cobalt catalysts. Brotz [10], Yang et al. [12] and Pannell et al. [13] defined the Fischer-Tropsch rate as the moles of hydrogen plus carbon monoxide converted per time per mass of catalyst (r g+Hj) Wang... [Pg.308]

Interesting videos and graphics keep people s attention. Case studies, requiring people to participate in providing solutions, tend to have better retention rates than lectures, which provide a summary of the law and the penalties associated with noncompliance. [Pg.450]


See other pages where Rate Laws A Summary is mentioned: [Pg.703]    [Pg.724]    [Pg.725]    [Pg.547]    [Pg.561]    [Pg.714]    [Pg.735]    [Pg.735]    [Pg.559]    [Pg.573]    [Pg.574]    [Pg.534]    [Pg.548]    [Pg.1153]    [Pg.703]    [Pg.724]    [Pg.725]    [Pg.547]    [Pg.561]    [Pg.714]    [Pg.735]    [Pg.735]    [Pg.559]    [Pg.573]    [Pg.574]    [Pg.534]    [Pg.548]    [Pg.1153]    [Pg.19]    [Pg.326]    [Pg.59]    [Pg.147]    [Pg.255]    [Pg.4698]    [Pg.255]    [Pg.297]    [Pg.586]    [Pg.254]    [Pg.88]    [Pg.561]    [Pg.455]    [Pg.481]    [Pg.4]    [Pg.137]   


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