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Rate laws, appropriate

The nickel ion dependence for the reaction between [Ni(NiL2)2]Cl2 and methyl iodide is such that a predissociation of the complex is suggested. The experimental rate law appropriate for this system is... [Pg.143]

Given a particular chemical reaction, which obeys a known set of reaction rate equations, we now seek to find out how the concentrations of the various species vary in space along the reactor, i.e. we wish to find the concentrations c(x). To show how this problem is equivalent to that of determining the time-dependent behaviour in a well-stirred closed vessel, we can take a general example for which a reactant A is converted to a product B. Let the rate law appropriate to a well-stirred closed vessel be... [Pg.239]

In this case, the denominator value should be taken from the rate law appropriate to this mechanism (Eq. 3.36). [Pg.41]

Since this is the first occasion we have had to examine the rates at which chemical reactions occur, a few remarks about mechanistic steps and rate laws seem appropriate. The reader who feels the need for additional information on this topic should consult the discussions which will be found in any physical chemistry text. [Pg.280]

Another reaction mechanism, which is conveniently mentioned under this heading, is due to Hill [479] who suggested that ions (atoms or molecules) frorh the product may move through the dislocation network of the reactant and activate potential nuclei, particularly in the vicinity of the reaction interface. Thus a reaction zone, within which potential nucleusforming sites are activated, is developed in front of an advancing interface. With appropriate assumptions, this reaction model provides an alternative explanation of the exponential rate law, eqn. (8), which in Sect. 3.2 was discussed with reference to chain reactions. [Pg.72]

Figure 22.1 A. Schema for a physiologically based pharmacokinetic model incorporating absorption in the stomach and intestines and distribntion to various tissues. B. Each organ or tissue type includes representation of perfusion (Q) and drug concentrations entering and leaving the tissue. Fluxes are computed by the product of an appropriate rate law, and permeable surface area accounts for the affinity (e.g., lipophilic drugs absorbing more readily into adipose tissue). Clearance is computed for each tissue based on physiology and is often assumed to be zero for tissues other than the gut, the liver, and the kidneys. Figure 22.1 A. Schema for a physiologically based pharmacokinetic model incorporating absorption in the stomach and intestines and distribntion to various tissues. B. Each organ or tissue type includes representation of perfusion (Q) and drug concentrations entering and leaving the tissue. Fluxes are computed by the product of an appropriate rate law, and permeable surface area accounts for the affinity (e.g., lipophilic drugs absorbing more readily into adipose tissue). Clearance is computed for each tissue based on physiology and is often assumed to be zero for tissues other than the gut, the liver, and the kidneys.
How appropriate is the power rate law for describing the kinetics of a catalytic reaction ... [Pg.402]

In order to test rate laws, a must be determined as a function of time using an appropriate experimental technique. If the reaction involves the loss of a volatile product as shown in Eq. (8.1), the extent of reaction can be followed by determining the mass loss either continuously or from sample weight at specific times. Other techniques are applicable to different types of reactions. After a has been determined at several reaction times, it is often instructive to make a graph of a versus time before the data are analyzed according to the rate laws. As will be shown later, one can often eliminate some rate laws from consideration because of the general shape of the a versus t curve. [Pg.256]

In this work, a detailed kinetic model for the Fischer-Tropsch synthesis (FTS) has been developed. Based on the analysis of the literature data concerning the FT reaction mechanism and on the results we obtained from chemical enrichment experiments, we have first defined a detailed FT mechanism for a cobalt-based catalyst, explaining the synthesis of each product through the evolution of adsorbed reaction intermediates. Moreover, appropriate rate laws have been attributed to each reaction step and the resulting kinetic scheme fitted to a comprehensive set of FT data describing the effect of process conditions on catalyst activity and selectivity in the range of process conditions typical of industrial operations. [Pg.294]

Similar substitution into Equations 16.10-16.12 gives masses of the basis entries at the end of a time step, Equations 16.13-16.14 yields the residual functions, and Equations 16.18-16.21 gives the entries in the Jacobian matrix. In evaluating the Jacobian, the derivatives dr /dnw and dr /dm, can be obtained by differentiating the appropriate rate law (Eqn. 17.9, 17.12, or 17.21), as discussed in Appendix 4, or their values determined just as efficiently by finite differences. [Pg.253]

The oxidation rate should, in principle, be described by a law using a rate constant independent of pH, as long as a single reaction mechanism is involved. The rate law (28.4) is unusual in that the rate varies with the concentration of the Mn11 component, rather than an individual species. If we hypothesize that the catalytic activity is promoted by a surface complex >MnOMnOH, a slightly different form of the rate law may be appropriate. Since the surface complex would... [Pg.421]

The primary use of chemical kinetics in CRE is the development of a rate law (for a simple system), or a set of rate laws (for a kinetics scheme in a complex system). This requires experimental measurement of rate of reaction and its dependence on concentration, temperature, etc. In this chapter, we focus on experimental methods themselves, including various strategies for obtaining appropriate data by means of both batch and flow reactors, and on methods to determine values of rate parameters. (For the most part, we defer to Chapter 4 the use of experimental data to obtain values of parameters in particular forms of rate laws.) We restrict attention to single-phase, simple systems, and the dependence of rate on concentration and temperature. It is useful at this stage, however, to consider some features of a rate law and introduce some terminology to illustrate the experimental methods. [Pg.42]

Investigate whether the rate law is of the form ( rA) = (-rB) = caCB, and state your conclusion, including, if appropriate, the value of k and its units. [Pg.84]

From the mechanism given in problem 7-8 for the decomposition of acetaldehyde, derive a rate law or set of independent rate laws, as appropriate, if H2 and C2Hs are major products (in addition to CH4 and CO). [Pg.172]

A stoichiometric analysis based on the species expected to be present as reactants and products to determine, among other things, the maximum number of independent material balance (continuity) equations and kinetics rate laws required, and the means to take into account change of density, if appropriate. (A stoichiometric table or spreadsheet may be a useful aid to relate chosen process variables (Fj,ch etc.) to a minimum set of variables as determined by stoichiometry.)... [Pg.442]

Equation (xi) must be numerically integrated, using either Ex(t) or E2 t), and the appropriate expressions for cA(t) and cD(t) (see E-Z Solve file ex20-5.msp). Table 20.1 gives the outlet concentration, conversion, yield, and selectivity obtained for each of the two cases, (d) Maximum-mixedness model For the maximum-mixedness model, the rate laws for A and D are substituted into Equation 20.4-6, and the two resulting ordinary differential equations (in dcA/dt and dcD/dt) must be numerically integrated. The respective equations are ... [Pg.507]

Within each stage, the amount of catalyst, W, may be calculated from equation 21.5-4, together with an appropriate rate law, and the energy equation 21.5-8. Optimization problems relating to minimizing W may be considered in terms of choice of values of r and fAi. [Pg.538]

In a typical situation, as illustrated in Figure 24.3, the composition and flow rate of each feed stream (gas at the bottom and liquid at the top) are specified, directly or indirectly this enables evaluation of the quantities pAin, cAin, cB in, L, and G. The unknown quantities to be determined, in addition to h (or I, the packed volume), are Pa,out and c, our The determination involves use of the rate law developed in Section 9.2 for an appropriate kinetics regime (1) reaction in bulk liquid only (relatively slow intrinsic rate of reaction), or (2) in liquid film only (relatively fast reaction), or (3) in both bulk liquid and liquid film. For case (2), cA = 0 throughout the bulk liquid, and the equations developed below for the more general case (3), cA 0, are simplified accordingly. [Pg.604]

The rate-law (2) can usually be established without too much difficulty by appropriate kinetic experiments, but it must be remembered that the same system may follow different rate-laws under different conditions, and it is evident that such kinetically complicated systems are generally unsuitable for attempts to determine the fundamental rate constants. However, a sufficient number of kinetically simple systems is now known which are much more useful for such studies. [Pg.416]

The rate law should be rearranged to k = Rate/[C102]2[0H ]. Then the appropriate values are entered into the equation. Using experiment 1 as an example ... [Pg.209]

Integration of the appropriate differential equations for the reaction scheme is straightforward, the resulting equations for the concentrations of A, B, and C as a function of time (see Chapter 3.4.2, Rate Laws with Explicit Solutions) are ... [Pg.143]

If the process of APIO is properly described by Equation (19), which infers the presence of a soluble Fe(III) intermediate species, it will be difficult to analyze this species directly, given the low levels that are expected. We must therefore develop mathematical approaches to estimating the isotopic composition of this component, as was done for DIR. The equations used in the previous chapter (Chapter lOA Beard and Johnson 2004) to describe abiotic Fe(II) oxidation are useful for illustrating possible isotopic fractionations that may occur during APIO. We will assume that the overall oxidation process occurs through a series of first-order rate equations, where relatively slow oxidation of FefTI) to a soluble Fe(III) component occurs, which we will denote as Fe(III)jq for simplicity. The oxidation step is followed by precipitation of Fe(III)jq to ferrihydrite at a much faster rate, which maintains a relatively low level of Fe(III)jq relative to Fe(II)jq. The assumption of first-order kinetics is not strictly valid for the experiments reported in Croal et al. (2004), where decreasing FefTI) contents with time do not closely follow either zeroth-, first-, or second-order rate laws. However, use of a first-order rate law allows us to directly compare calculations here with those that are appropriate for abiologic Fe(II) oxidation, where experimental data are well fit to a first-order rate law (Chapter lOA Beard and Johnson 2004). [Pg.386]

In this section, you learned how to express reaction rates and how to analyze reaction rate graphs. You also learned how to determine the average rate and instantaneous rate of a reaction, given appropriate data. Then you examined different techniques for monitoring the rate of a reaction. Finally, you carried out an investigation to review some of the factors that affect reaction rate. In the next section, you will learn how to use a rate law equation to show the quantitative relationships between reaction rate and concentration. [Pg.276]

Attention is now directed to reactions that show a nonlinear plot of the appropriate function or that have rate laws that are altered with changes in the concentration of the species involved in the reaction. Such deviations are usually associated with concurrent and consecutive reactions. [Pg.16]

Since proton exchange is usually measured by nmr methods in D2O (Secs. 3.9.5 and 3.9.6), the more appropriate rate law is... [Pg.362]

The above rate law agrees with the given one and hence this mechanism seems most appropriate. [Pg.276]

The rate constant, k, is simply the constant of proportionality in the expression relating the rate of a reaction to the concentrations of reactants and/or products, each expressed with the appropriate exponent. The order of a reaction is defined as the sum of the exponents in the rate law. Thus reaction (4) is (1 + 1) = second order. The order with respect to each species appearing in the rate law is the exponent of the concentration of that species thus reaction (4) is first order in both 03 and NO. [Pg.131]

Rate laws, which we cover in Chapter 14, relate reaction rates to the concentrations of reactants. Which rate law is appropriate depends on the kind of reaction involved ... [Pg.284]

For appropriate relative values of the two denominator terms, this expression will reduce to the simple second-order rate law. Equation 9 may be rewritten in the form... [Pg.239]

With the full Arrhenius rate law, an extra unfolding parameter y is introduced. Even then, however, the appropriate stationary-state condition and its derivatives for the winged cusp cannot be satisfied simultaneously (at least not for positive values of the various parameters). Thus we do not expect to find all seven patterns. [Pg.206]


See other pages where Rate laws, appropriate is mentioned: [Pg.625]    [Pg.641]    [Pg.17]    [Pg.693]    [Pg.250]    [Pg.272]    [Pg.75]    [Pg.408]    [Pg.542]    [Pg.542]    [Pg.619]    [Pg.681]    [Pg.80]    [Pg.81]    [Pg.528]    [Pg.11]    [Pg.664]    [Pg.241]    [Pg.78]   
See also in sourсe #XX -- [ Pg.113 , Pg.114 , Pg.116 ]




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