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Single Step Irreversible Reaction

By applying Eqs.(3-6) and (3-10), the following one step transition probability matrix is obtained  [Pg.213]

It should be noted that exact solutions for the above models are available in refs.[32, vol.l, p.361 34, pp.4-5, 4-6]. For At = 0.01, the agreement between the Markov chain solution and the exact solution is Dmax = 0.4% and Dmean = 0.2%. [Pg.215]

The following one step transition probability matrix is obtained  [Pg.215]


More complicated interpretations of B -1- M -> C -h M in the limit >>1 can be made that still fall in the realm of simplified modeling, for example, the two-step Lindemann mechanism, B M <=> B + M B -> C [8]. However, such interpretations haven t been shown to lead to better agreement with observations for homogeneous energetic solids than the single step, irreversible reaction and since they represent an additional level of complexity they are not considered here. [Pg.240]

Most of the numerical calculations have been based on the use of (i) single-step irreversible reaction models and (li) the assumption of a poly tropic gas mixture. In order to catch the essential features of real detonations and detonation initiation phenomena, Lee and Higgins [7] suggested that one should use (i) chemical mechanisms with at least two or three reaction steps and (li) thermodynamics relations for gas mixtures at high temperatures. [Pg.391]

The flow involves fuel, F, issuing from a central slot of width D with an oxidizer, O, co-flow with both streams at the reference temperature, Tq. A global single-step, irreversible, exothermic chemical reaction of the type F + rO —> (1 -f r)P with an Arrhenius reaction rate coefiicient is assumed. A hot layer of combustion products, P, at the inlet serves to separate the fuel and oxidizer streams and acts as an ignition source. The inlet conditions for the velocity, temperature, and composition are shown in Fig. 10.2. The ratio of the inlet velocities of the fuel to oxidizer streams is chosen as 4. Inlet velocity forcing is used to induce early roll-up and pairing of the jet shear layer vortices. [Pg.164]

If a resistor is added in series with the parallel RC circuit, the overall circuit becomes the well-known Randles cell, as shown in Figure 4.11a. This is a model representing a polarizable electrode (or an irreversible electrode process), based on the assumptions that a diffusion limitation does not exist, and that a simple single-step electrochemical reaction takes place on the electrode surface. Thus, the Faradaic impedance can be simplified to a resistance, called the charge-transfer resistance. The single-step electrochemical reaction is described as... [Pg.154]

For a single, elementary, irreversible, reaction step, d> is given by equation (3) and equations (4) and (14) imply that... [Pg.557]

The propellant is assumed to undergo an irreversible thermal decomposition process in the condensed phase. The simplest description of this process is a single-step, unimolecular reaction with the initial reactant species-A (formula weight W) going to intermediate species-B (same formula weight W) as shown in Fig. 1,... [Pg.228]

Chronoabsorptometry has been applied to the determination of heterogeneous electron-transfer parameters in single-step irreversible [55] and quasi-irreversible kinetics [56] and in double potential step modes [57]. In the case of a single potential step for the reaction... [Pg.497]

Figure 6.7 shows a typical special feature of the polarization curves. In the case of reversible reactions (curve 1), the anodic and cathodic branches of the curve form a single step or wave. In the case of irreversible reactions, independent, anodic and cathodic, waves develop, each having its own inflection or half-wave point. The differences between the half-wave potentials of the anodic and cathodic waves will be larger the lower the ratio fH. ... [Pg.97]

Depending on the mechanism of irreversible reaction, inactivation can appear to proceed through either a single-step or a two-step mechanism (Figure 8.2). In the case of nonspecific affinity labels (see Section 8.2) many amino acid residues on the enzyme molecule, and on other protein molecules in the sample, can be covalently modified by the affinity label. Not every modification event will lead to inactiva-... [Pg.216]

Thus a plot of fcobs as a function of [/] will yield a linear plot with the y-intercept = kog and slope = k (Figure A1.6). This is exactly the behavior we encountered in Chapters 6 and 8 for slow binding and irreversible inhibitors that bind to their target enzymes in a single-step reaction. [Pg.259]

The present chapter will cover detailed studies of kinetic parameters of several reversible, quasi-reversible, and irreversible reactions accompanied by either single-electron charge transfer or multiple-electrons charge transfer. To evaluate the kinetic parameters for each step of electron charge transfer in any multistep reaction, the suitably developed and modified theory of faradaic rectification will be discussed. The results reported relate to the reactions at redox couple/metal, metal ion/metal, and metal ion/mercury interfaces in the audio and higher frequency ranges. The zero-point method has also been applied to some multiple-electron charge transfer reactions and, wheresoever possible, these results have been incorporated. Other related methods and applications will also be treated. [Pg.178]

It is readily apparent that equation 8.3.21 reduces to the basic design equation (equation 8.3.7) when steady-state conditions prevail. Under the presumptions that CA in undergoes a step change at time zero and that the system is isothermal, equation 8.3.21 has been solved for various reaction rate expressions. In the case of first-order reactions, solutions are available for both multiple identical CSTR s in series and individual CSTR s (12). In the case of a first-order irreversible reaction in a single CSTR, equation 8.3.21 becomes... [Pg.278]

In an irreversible reaction, the rate controlling process is usually a single electron transfer step with a rate determined by Equation 1.8. The corresponding po-larographic wave is then described by Equation 1.18 where kconv is the rate constant for electron transfer at the potential of the reference electrode. For an irreversible... [Pg.17]

Such a complex behavior of x(AG ) in the presence of the triplet channel is smoothed at faster diffusion when ko is closer to the maximal value of the recombination constants. In this case there is a single step border [dashed line in Fig. 3.81(a)] between the irreversible (to the left) and reversible (to the right) reactions. The position of this border essentially depends on the true height of k,. In Figure 3.81 (Vi) one can see how the border marked by this line is shifted to the right with the increasing rate of triplet recombination. [Pg.341]

As long as the steps of the sequence are irreversible, the original reactant behaves as in single-step decay, regardless of the reaction orders. Concentration histories of later members in sequences that include steps of orders other than first have been derived for only a few simple cases and are unwieldy even for these [19,20], Here, numerical solution on a computer is preferable. However, two general rules can be stated ... [Pg.109]

In the laboratory, amides and esters are usually prepared from the acid chloride rather than from the acid itself. Both the preparation of the acid chloride and its reactions with ammonia or an alcohol are rapid, essentially irreversible reactions. It is more convenient to carry out these two steps than the single slow, reversible reaction with the acid. For example n... [Pg.666]

Reactions are seldom completely irreversible, and a rigorous description of the kinetics of a second-order reaction that occurs in a single step must take into account the reverse reaction. The rate of the reaction is the difference between the forward rate and the reverse rate ... [Pg.884]

Parallel reactions single and consecutive-irreversible reaction steps. [Pg.211]

PARALLEL REACTIONS SINGLE AND CONSECUTIVE IRREVERSIBLE REACTION STEPS... [Pg.250]

Fig. 1 Problem schematic for burning homogeneous propellant showing condensed phase (surface) reaction zone, gas phase reaction zone and corresponding steady-state temperature profiles. Propellant is fed from left at surface regression rate r. Simplified kinetics description has propellant (A) decomposing in condensed phase to intermediate species (B) via zero-order, high activation energy, irreversible single-step reaction, and (B) reacting to (C) in gas phase via second-order (overall), irreversible single-step reaction. Fig. 1 Problem schematic for burning homogeneous propellant showing condensed phase (surface) reaction zone, gas phase reaction zone and corresponding steady-state temperature profiles. Propellant is fed from left at surface regression rate r. Simplified kinetics description has propellant (A) decomposing in condensed phase to intermediate species (B) via zero-order, high activation energy, irreversible single-step reaction, and (B) reacting to (C) in gas phase via second-order (overall), irreversible single-step reaction.

See other pages where Single Step Irreversible Reaction is mentioned: [Pg.211]    [Pg.213]    [Pg.211]    [Pg.213]    [Pg.158]    [Pg.556]    [Pg.185]    [Pg.103]    [Pg.7]    [Pg.332]    [Pg.44]    [Pg.204]    [Pg.63]    [Pg.13]    [Pg.165]    [Pg.7]    [Pg.43]    [Pg.234]    [Pg.14]    [Pg.170]    [Pg.1083]    [Pg.99]    [Pg.143]    [Pg.8]    [Pg.245]    [Pg.47]   


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