Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Diffusion Controlled Reactions Neutral Species

From Sect. 2.4.1 the time dependent survival probability for a neutral pair is known to be [Pg.101]

In the simulation if C/(0,1] a/r, the particles have escaped and will never recombine. In this situation, the recombination time Tg = tmsa-Otherwise a separate Tg is generated from Eq. (4.36) for aU possible encountering pairs. [Pg.101]

In the simulation not all encounters will result in reaction due to some constraint. The two most common reasons for the encountering pairs to not react are (i) the reactions are partially diffusion controlled and the boundary is not reactive, or (ii) the radical pair is in the wrong spin state to react. In either case a careful treatment for the reflection is required to correctly model the subsequent kinetics, something which is not easily attainable in the IRT framework as the diflusive trajectories are not tracked. This section now presents a new analytical method of finding the distance of the radical pair following an unsuccessful encounter. [Pg.102]

To generate a reflected distance it is necessary to know the probability distribution function for a pair started at contact subject to the boundary being reflective. Using the renewal theorem, the transition density of reflecting at a and separating to a distance r is [Pg.102]

This equation can be inverted to give the probability distribution in the time domain [Pg.103]


Partially Diffusion Controlled Reactions Neutral Species... [Pg.109]

Green and Pimblott (1989) have extended the IRT model to partially diffusion-controlled reactions between neutrals. They derive an analytical expression that involves an additional parameter, namely the reaction velocity at encounter. For reactions between charged species, W generally cannot be given analytically but must be obtained numerically. Furthermore, numerical inversion to get t then... [Pg.222]

The motion of molecules in a liquid has a significant effect on the kinetics of chemical reactions in solution. Molecules must diffuse together before they can react, so their diffusion constants affect the rate of reaction. If the intrinsic reaction rate of two molecules that come into contact is fast enough (that is, if almost every encounter leads to reaction), then diffusion is the rate-limiting step. Such diffusion-controlled reactions have a maximum bimolecular rate constant on the order of 10 ° L mol s in aqueous solution for the reaction of two neutral species. If the two species have opposite charges, the reaction rate can be even higher. One of the fastest known reactions in aqueous solution is the neutralization of hydronium ion (H30 ) by hydroxide ion (OH ) ... [Pg.775]

For reactions between species of similar size in water at 25 C, eq. (9.24) leads to a value of the diffusiou-controUed rate constaut for neutral species of 7X10 dm moF sec. This is probably au underestimate, and in Table 9.5, some experimental rate constants are given for diffusion-controlled reactions in water. [Pg.233]

In this section the foundations of the theory underlying chemical kinetics are presented. Based on the diffusion equation to describe Brownian motion together with Smoluchowski s theory [ 1, 2], a thorough derivation of the bulk reaction rate constant for neutral species for both diffusion and partially diffusion controlled reactions is presented. This theory is then extended for charged species in subsequent sections. [Pg.25]

Radicals are normally very reactive, often reacting under diffusion control (second-order rate constant ca. 109 dm3 mol-1 s 1) with other species (radicals, neutral molecules or ions), Scheme 10.1. However, although radical-radical reactions normally have very high second-order rate constants, radical concentrations are generally very low. Therefore, radical-neutral molecule or radical-ion reactions with smaller rate constants take place preferentially because the concentrations of neutral molecules or ions can be very high. Radical... [Pg.262]

As outlined above (p. 3), a reaction can be subject to microscopic diffusion control only if one of the reactive intermediates is formed from an inactive precursor in the reaction mixture. There are two sets of conditions which have provided evidence for microscopic diffusion control in nitration. One concerns solutions of nitric acid in aqueous mineral acids or organic solvents for, in most of these solutions, the stoicheiometric nitric acid is mainly present as the molecular species in equilibrium with a very small concentration of nitronium ions. A reaction between a substrate and a nitronium ion from this equilibrium concentration can, in principle, be subject to microscopic diffusion control. The other set of conditions is when the substrate is mainly present as the protonated form SH+ but when reaction occurs through a very small concentration of the neutral base S. A reaction between the neutral base and a nitronium ion can then, in principle, be subject to microscopic diffusion control even if the nitronium ions are the bulk component of the HN03/N0 equilibrium. In considering the evidence for microscopic diffusion control it is convenient to consider separately the reactions of those species involved in prototopic equilibria. [Pg.24]

Several reactions have been reported for disulfide radical cations generated in water by pulse radiolysis techniques. These species are oxidants and undergo one-electron transfer with Fe(CN) at near diffusion controlled rates (ca. 1010 M 1s 1) [456,457], with Fe2+ with rate constants [456] the order of 106 M 1s 1 with 1 [458] and with RS [484]. Disulfide radical cations, like other sulfur radical cations, do not react with 02 [399]. On the basis of the second order decomposition of these radical cations in acidic and neutral aqueous solutions, their disproportionation to the corresponding dication as shown in Eq. (55) has been suggested [456] ... [Pg.72]

We now discuss some of the main features of LLPTC models developed for reaction under neutral conditions. Evans and Palmer (1981) were among the first to consider the effect of diffusion and mass transfer inPTC. They considered PTC in liquid-liquid systems by considering two well-mixed bulk phases of uniform composition separated by a uniform stagnant mass-transfer layer at the interface, and set up equations for bulk phase species balance and mass conservation equations for simultaneous diffusion and reaction in the film. Dynamics of the interaction between reaction and diffusion were studied under these assumptions for two special cases (a) reaction which is pseudo-first-order in the quaternary ion-pair (b) mass-transfer controlled instantaneous reaction. [Pg.11]

If the longer-lived species are indeed Cl atom-solute complexes, they may be formed at diffusion controlled rates with k — lO Af"1 sec."1. In the presence of 0.1M solute these species are observed directly after the pulse, so the Cl atoms must be formed in less than 1 nsec. The decay of the positive ion is much longer than this, and it seems that the Cl atoms are not formed by the ion-neutralization reaction. [Pg.356]

The diffusion-controlled rate constant in water (tj = 0.890 mPa s) is 7.4 X 10 mol dm s values in a variety of solvents are given in the literature [34], This equation is valid for reaction between neutral species of the same size. The effect of charge and size is discussed in standard textbooks on chemical kinetics [61], Diffusional quenching is often termed dynamic quenching because it involves movement. The effect of dynamic quenching is a reduction in both the quantum yields of competing processes, such as emission from the donor, and the lifetime of the donor excited-state. [Pg.77]

Amperometric sensors are based on electrochemical reactions which are governed by the diffusion of the electroactive species through a barrier. 129 The barrier usually consists of a hole (see Figure 10.11a) or a porous neutral layer. The control of the gas inflow by an electrochemical method was proposed recently. 2 The voltage is fixed on the diffiision plateau of the I(U) curve (Figure 10.1 lb). For a reaction limited by the mass transport process, the general flux equation in a one-dimensional model is... [Pg.358]


See other pages where Diffusion Controlled Reactions Neutral Species is mentioned: [Pg.101]    [Pg.101]    [Pg.287]    [Pg.200]    [Pg.97]    [Pg.131]    [Pg.220]    [Pg.227]    [Pg.2581]    [Pg.2637]    [Pg.90]    [Pg.630]    [Pg.171]    [Pg.128]    [Pg.105]    [Pg.3006]    [Pg.64]    [Pg.237]    [Pg.110]    [Pg.574]    [Pg.235]    [Pg.79]    [Pg.122]    [Pg.57]    [Pg.923]    [Pg.40]    [Pg.200]    [Pg.17]    [Pg.304]    [Pg.36]    [Pg.90]   


SEARCH



Diffusing species

Diffusion control

Diffusion controlled

Diffusion reaction control

Diffusion reactions

Diffusion-controlled reactions

Diffusivity reactions

Neutral species

Neutralization reactions

Reaction species

© 2024 chempedia.info