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Space integral rate

Since both G, and Gi are known from the boundary conditions defining the specific flame problem (Section 4), the space integral rate provides a means of extracting the current value of the product (MyA) from an unsteady-state... [Pg.30]

The source term or space integral rate S, may now be expressed sufficiently accurately as... [Pg.62]

Our next task is thus to set up the microintegral equations corresponding with expression (4.55) for the u and b boundary half-intervals. We commence at Eq. (4.22) and proceed as before. In the flame context, it is assumed that no chemical reaction takes place in the volume of either of the end half-intervals, that is, that the space integral rates there are zero. This is reasonable, since there should be no major reaction near free boundaries, while walls are presumed to be perfect sinks for free radicals. [Pg.68]

Convergence to a steady rate of propagation may be monitored by the approach of the space integral rate over the whole flame to a constant value (cf. Section 2.6). The steady-state burning velocity My [or the product (M A)] may be obtained directly from Eq. (4.71)... [Pg.74]

There are two possible methods of approach. Either the space integral rates Siu and the associated derivative terms a are evaluated at the beginning of the time interval, and the dependent variables are updated together at the end of the interval or the appropriate 5, and Sjy a are evaluated immediately prior to the solution of each equation and each dependent variable is updated immediately after the solution of its equation. When using the latter method, the order of solution of the equations becomes important. The most satisfactory order treats the most reactive free radicals first, then less reactive intermediates, initial reactants, reaction products and inert species in that order, and finally the enthalpy. The latter method is potentially the more economical computationally, but it forfeits precise chemical conservation during single time steps on the approach to the steady state. This has been found to cause instability in certain diffusion flame problems to be outlined in Section 7.2(b). The former method does not suffer from this disadvantage. [Pg.78]

The bulk of the infomiation about anhannonicity has come from classical mechanical calculations. As described above, the aidiannonic RRKM rate constant for an analytic potential energy fiinction may be detemiined from either equation (A3.12.4) [13] or equation (A3.12.24) [46] by sampling a microcanonical ensemble. This rate constant and the one calculated from the hamionic frequencies for the analytic potential give the aidiannonic correctiony j ( , J) in equation (A3.12.41). The transition state s aidiannonic classical sum of states is found from the phase space integral... [Pg.1021]

QTST is predicated on this approach. The exact expression 50 is seen to be a quantum mechanical trace of a product of two operators. It is well known, that such a trace can be recast exactly as a phase space integration of the product of the Wigner representations of the two operators. The Wigner phase space representation of the projection operator limt-joo %) for the parabolic barrier potential is h(p + mwtq). Computing the Wigner phase space representation of the symmetrized thermal flux operator involves only imaginary time matrix elements. As shown by Poliak and Liao, the QTST expression for the rate is then ... [Pg.31]

In reactors in which the concentrations of reactants and products are uniform in space, the rate is the same on all parts of the catalyst surface at any specified time. In integral flow reactors, however, the rate on each element of the catalyst bed varies along the bed. [Pg.372]

Again, the quantum mechanical expressions can be written in a form that is analogous to the classical expressions for the rate constant given in Section 5.1, remembering that a classical phase-space integral is equivalent to a quantum mechanical trace [9], and classical functions of coordinates and momenta are equivalent to the corresponding quantum mechanical operators. [Pg.137]

In the general case of a spatially inhomogeneous system, the total rate of energy dissipation is described by the space integral ... [Pg.118]

Introducing these standard finite volume space integrations, and changing the order of integration in the rate of change term we get ... [Pg.1018]

The main attraction of using the integral approach in conventional studies is that it avoids the need to measure rates of reaction. Instead, the output conversions from several isothermal runs at different space times are plugged into the integrated rate expression and the rate parameters are optimized as simple constants for a given temperature. Since there usually are few parameters in a rate expression, a few runs will suffice to define all the constants at one temperature certainly, fewer runs than would be necessary to make valid estimates of rates from a plot of X vs. x. Repeating this procedure at several temperatures yields a set of constants suitable for plotting on an Arrhenius plot. This procedure minimizes the number of isothermal runs necessary to obtain the rate parameters. [Pg.262]

We now apply the entropy inequality (1.42) to our continuous body (or arbitrary part of it). Because the integral in (1.42) may be understood (by definition of heat distribution) as time and space integral we can formulate an entropy inequality using the entropy rate, heating and corresponding densities of these quantities (cf. end of Sect. 1.4 and the way we obtained (2.2) again it is possible to proceed more naturally, see Rems. 7,14 and 18) [11, 18, 35, 41]. Therefore entropy may be expressed if we introduce the specific entropy s as a primitive objective scalar. Because the heating now contains surface and volume parts with densities q and Q (cf. (3.97)) and because the absolute temperature is now scalar field T = T(x, t), assumed to be objective, it follows that the entropy inequality may be formulated as (we use (3.100))... [Pg.97]

D + CH3 CDH3 The recombination reaction of CH3 with H(D) has frequently been studied by FTST approaches [1,6,4,8] and paper I. In all these publications, the ab initio fully dimensional CH4 potential energy surface of Hase Qt al [9] has been used. These studies have shown fliat canonical ST overestimates microcanonical FTST by only 5% to 9% for temperatures from 300 K to 2000 K. Thus a canonical theoiy is largely reliable in comparisons to experiment. In paper I, rate constant calculations for H+CH3 via Eq. (11) reproduced previous canonical FTST studies with full numerical phase space integrations. However, the only reliable measurements of the high pressure recombination rate constant for this system are for the D+CH3 isotopic variant [10]. Here we apply Eq. (11) to this variant. [Pg.207]

The PST calcrrlations of the association rates for the ion-molecule reactions can be carried out using programs such as VariFlex [86]. Though the main aim of this program is the calculation of rates for barrierless reactions, it also allows convenient estimates of the rates using PST. The program employs Monte Carlo phase space integration to evaluate the statistical functions. [Pg.55]

In the case of combined device (i.e., filtration-flotation water treatment under recirculation conditions), it is important to know the values of integrated constants of the filtration process, bioflltration process, bubble-flhn extraction process, gas exchange absorption process, and ion separation process in the functional units of combined device, that is, in the filter and in the bubble-film extractor, operating separately. The initial parameters for the device analysis are the required purification degree and treating time. And the calculated parameters are the integrated rate constants of such processes as filtration, biofiltration, flotation, bubble absorption, and dimensions of reaction spaces. [Pg.505]

The selection of the initial conditions for classical trajectories is designed to simulate the experimental conditions of interest. The properties of interest are averages, for example, the thermal rate coefficient is an average of the reaction probabilities over all of the volume of the phase space available to the system at a particular temperature. (For a more explicit discussion of the details of these averages, see the reviews by Tmhlar and Muckerman and by Raff and Thompson. ) These averages can be written as phase space integrals of the type... [Pg.3060]

When the unsteady-state equations are being integrated forward in time either towards the Eulerian steady state or towards the Lagrangian steady propagation rate, a criterion is required for deciding when the steady situation is achieved. In both cases this is provided by the space integral reaction rates qiA dy, which for sufficiently small finite difference intervals may be replaced by the summations x y)n or an equivalent quantity, where A dy) is the volume of the nth element and A a weighted mean area within the element. For the quasi-one-dimensional steady-state flame we have from Eq. (2.12)... [Pg.30]


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