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Chemical reactions reaction velocity

Theoretical investigations of the modification phenomenon have been carried out by Roginskil and Vol kenshteln (342,418,419,420,421,423). Their work has been based upon the electronic theory of catalysis which utilizes greatly present-day knowledge of quantum chemistry and those theories of the solid state which deal with processes occurring within crystalline materials. On the basis of these concepts it is possible to treat the problems involved in the conversion of molecules adsorbed on a solid surface. The adsorbed molecule and the solid are treated as a unified system, the electrons of the lattice participating in bonding and subsequently chemical reaction. The velocity of the chemical reaction is dependent upon the electronic properties of the solid and reactants involved. [Pg.264]

Throughout the range of chemical reactions whose velocities can be measured there is a clearly marked correlation between the value of E and the temperature at which the rate attains some specified... [Pg.361]

We shall again consider the reaction (162), and to simplify matters somewhat, we shall assume ideality in the solution and in the interphase. The problem is usually handled as follows one first takes the particular case of a zero electric potential difference from metal to solution (from a to c in our notations) and the electrode process is then regarded as a purely chemical reaction of velocity... [Pg.39]

Since the exact densities of various chemically active spjecies and their diffusion coefficients are not known, methane diffusion in argon is simulated in order to have some hints about the diffusion of various chemically active sp>ecies. Simulated results for methane diffusion in the figure 15 show that it takes about 10 to 20 ms for a chemically active sp>ecies generated in the filament, which is ap>proximately placed at the middle of the tube, to reach the tube surface. During this transpwrt process, it may imdergo several chemical reactions. Gas velocity is 1.4 m-s-i for the flow rate of 2.4 shn. Hence, in the duration of 10 to 20 ms, neutral radicals will be moved to a distance of 1.5 to 3 cm along the axis of the tube. [Pg.243]

Note that, although a nonzero affinity means there is a driving force for chemical reactions, the velocity d i /dt at which these chemical reactions will occur is not specified by the affinity s value. The rates of chemical reactions are usually known through empirical means and they depend on one or more mechanisms. [Pg.110]

The oxidized chemical waves themselves are a consequence of the coupling between diffusion and chemical reaction. Their velocity is determined by the diffusion coefficient of the autocatalytic species HBrO and the rate constant of its formation in the autocatalytic reaction mentioned above ... [Pg.490]

Here is a vector of reaction velocities which are usually nonlinear functions of tire chemical... [Pg.3055]

The Restart check box can be used in ctiii junction with the explicit editing of a IIIX file to assign completely user-specified initial velocities. This may be useful in classical trajectory analysis of chemical reactions where the initial velocities and directions of the reactants are varied to statistically determine the probability of reaction occurring, or n ot, in the process of calculating a rate con -Stan t. [Pg.313]

Computer Models, The actual residence time for waste destmction can be quite different from the superficial value calculated by dividing the chamber volume by the volumetric flow rate. The large activation energies for chemical reaction, and the sensitivity of reaction rates to oxidant concentration, mean that the presence of cold spots or oxidant deficient zones render such subvolumes ineffective. Poor flow patterns, ie, dead zones and bypassing, can also contribute to loss of effective volume. The tools of computational fluid dynamics (qv) are useful in assessing the extent to which the actual profiles of velocity, temperature, and oxidant concentration deviate from the ideal (40). [Pg.57]

The development of combustion theory has led to the appearance of several specialized asymptotic concepts and mathematical methods. An extremely strong temperature dependence for the reaction rate is typical of the theory. This makes direct numerical solution of the equations difficult but at the same time accurate. The basic concept of combustion theory, the idea of a flame moving at a constant velocity independent of the ignition conditions and determined solely by the properties and state of the fuel mixture, is the product of the asymptotic approach (18,19). Theoretical understanding of turbulent combustion involves combining the theory of turbulence and the kinetics of chemical reactions (19—23). [Pg.517]

There is no sharp dividing hne between pure physical absorption and absorption controlled by the rate of a chemic reaction. Most cases fall in an intermediate range in which the rate of absoration is limited both by the resistance to diffusion and by the finite velocity of the reaction. Even in these intermediate cases the equihbria between the various diffusing species involved in the reaction may affect the rate of absorption. [Pg.615]

Vibrofluidizatlon It is possible to fluidize a bed mechanically by imposing vibration to throw the particles upward cychcaUy. This enables the bed to operate with either no gas upward velocity or reduced gas flow. Entrainment can also be greatly reduced compared to unaided fluidization. The technique is used commercially in drying and other applications [Mujumdar and Erdesz, Drying Tech., 6, 255-274 (1988)], and chemical reaction applications are possible. See Sec. 12 for more on diying applications of vibrofluidization. [Pg.1562]

Deflagration A propagating chemical reaction of a substance in which the reaction front advances into the unreacted substance at less than the sonic velocity in the unreacted material. Where a blast wave is produced that has the potential to cause damage, the term explosive deflagration may be used. [Pg.160]

Although it does not physically explain the nature of the removal process, deposition velocity has been used to account for removal due to impaction with vegetation near the surface or for chemical reactions with the surface. McMahon and Denison (12) gave many deposition velocities in their review paper. Examples (in cm s ) are sulfur dioxide, 0.5-1.2 ozone, 0.1-2.0 iodine, 0.7-2.8 and carbon dioxide, negligible. [Pg.287]


See other pages where Chemical reactions reaction velocity is mentioned: [Pg.477]    [Pg.346]    [Pg.346]    [Pg.41]    [Pg.231]    [Pg.251]    [Pg.341]    [Pg.418]    [Pg.664]    [Pg.958]    [Pg.2059]    [Pg.3055]    [Pg.330]    [Pg.121]    [Pg.373]    [Pg.411]    [Pg.79]    [Pg.460]    [Pg.216]    [Pg.116]    [Pg.117]    [Pg.3]    [Pg.211]    [Pg.379]    [Pg.380]    [Pg.383]    [Pg.324]    [Pg.518]    [Pg.287]    [Pg.673]    [Pg.1209]    [Pg.1424]    [Pg.1442]    [Pg.1633]    [Pg.2425]   
See also in sourсe #XX -- [ Pg.389 , Pg.392 , Pg.393 , Pg.394 , Pg.395 ]




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