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Specific reaction parameters

The various processes listed above can be described quantitatively by their respective functional terms, each requiring a unique set of parameters. Fortunately, many parameters are used simultaneously for many or all of the above reactions, like temperature or concentrations. In general, the parameters can be divided into system-specific parameters (subdivided into the stationary state and the dynamic evolution) and into reaction-specific parameters. Many of these parameters also depend on the chemical or physical models applied to the system. The resulting very complex pattern usually has to be simplified when it comes to integrated modelling exercises of contaminant reaction paths and migration, based on coupled transport codes. [Pg.81]

The major reasons for using intrinsic fluorescence and phosphorescence to study conformation are that these spectroscopies are extremely sensitive, they provide many specific parameters to correlate with physical structure, and they cover a wide time range, from picoseconds to seconds, which allows the study of a variety of different processes. The time scale of tyrosine fluorescence extends from picoseconds to a few nanoseconds, which is a good time window to obtain information about rotational diffusion, intermolecular association reactions, and conformational relaxation in the presence and absence of cofactors and substrates. Moreover, the time dependence of the fluorescence intensity and anisotropy decay can be used to test predictions from molecular dynamics.(167) In using tyrosine to study the dynamics of protein structure, it is particularly important that we begin to understand the basis for the anisotropy decay of tyrosine in terms of the potential motions of the phenol ring.(221) For example, the frequency of flips about the C -C bond of tyrosine appears to cover a time range from milliseconds to nanoseconds.(222)... [Pg.52]

The combined use of the modem tools of surface science should allow one to understand many fundamental questions in catalysis, at least for metals. These tools afford the experimentalist with an abundance of information on surface structure, surface composition, surface electronic structure, reaction mechanism, and reaction rate parameters for elementary steps. In combination they yield direct information on the effects of surface structure and composition on heterogeneous reactivity or, more accurately, surface reactivity. Consequently, the origin of well-known effects in catalysis such as structure sensitivity, selective poisoning, ligand and ensemble effects in alloy catalysis, catalytic promotion, chemical specificity, volcano effects, to name just a few, should be subject to study via surface science. In addition, mechanistic and kinetic studies can yield information helpful in unraveling results obtained in flow reactors under greatly different operating conditions. [Pg.2]

Figure 5. Measurement and analysis of steady-state i— V characteristics, (a) Following subtraction of ohmic losses (determined from impedance or current-interrupt measurements), the electrode overpotential rj is plotted vs ln(i). For systems governed by classic electrochemical kinetics, the slope at high overpotential yields anodic and cathodic transfer coefficients (Ua and aj while the intercept yields the exchange current density (i o). These parameters can be used in an empirical rate expression for the kinetics (Butler—Volmer equation) or related to more specific parameters associated with individual reaction steps.(b) Example of Mn(IV) reduction to Mn(III) at a Pt electrode in 7.5 M H2SO4 solution at 25 Below limiting current the system obeys Tafel kinetics with Ua 1/4. Data are from ref 363. (Reprinted with permission from ref 362. Copyright 2001 John Wiley Sons.)... Figure 5. Measurement and analysis of steady-state i— V characteristics, (a) Following subtraction of ohmic losses (determined from impedance or current-interrupt measurements), the electrode overpotential rj is plotted vs ln(i). For systems governed by classic electrochemical kinetics, the slope at high overpotential yields anodic and cathodic transfer coefficients (Ua and aj while the intercept yields the exchange current density (i o). These parameters can be used in an empirical rate expression for the kinetics (Butler—Volmer equation) or related to more specific parameters associated with individual reaction steps.(b) Example of Mn(IV) reduction to Mn(III) at a Pt electrode in 7.5 M H2SO4 solution at 25 Below limiting current the system obeys Tafel kinetics with Ua 1/4. Data are from ref 363. (Reprinted with permission from ref 362. Copyright 2001 John Wiley Sons.)...
While chamber contamination and the presence of unknown surface reactions are probably the most important problems in extrapolating smog chamber data to atmospheric conditions, other minor problems exist as well. These include the need to measure carefully and frequently a number of chamber-specific parameters such as the decay rate of 03 on the chamber walls and the initial formation of HONO. Such chamber-specific parameters raise the question again of how best to modify these parameters to describe ambient air. [Pg.882]

The best way to compare the catalytic efficiencies of different enzymes or the turnover of different substrates by the same enzyme is to compare the ratio kcat/Km for the two reactions. This parameter, sometimes called the specificity constant, is the rate constant for the conversion of E + S to E + P. When [S] << Km, Equation 6-26 reduces to the form... [Pg.207]

Table 1 presents as an example the experimental dependences of kinetic parameters of the reaction, structural parameters of the network and some physico-mechanical characteristics on the molar fraction of monofunctional molecules in the reactant mixture, which is specific of FTD in the given case. As can be seen, the presence of monofunctional molecules, even in minor amounts (only 3-10%), exerts a strong influence on the kinetic and physico-mechanical parameters. [Pg.133]

When the kinetic model has been established, it is tested against data from selected non-reaction-specific or global experiments. These experiments provide information on the behavior of certain reaction systems, for instance mixtures of fuel and oxidizer. They usually require a complex chemical kinetic model for interpretation. The process must be studied either under transport-free conditions, such as in plug-flow or stirred-tank reactors, or under conditions in which the transport phenomena can be modeled very precisely, such as under laminar flow conditions. This way computer predictions become influenced primarily by parameters in the chemical kinetic model. [Pg.566]

Model Equations to Describe Component Balances. The design of PVD reacting systems requires a set of model equations describing the component balances for the reacting species and an overall mass balance within the control volume of the surface reaction zone. Constitutive equations that describe the rate processes can then be used to obtain solutions to the model equations. Material-specific parameters may be estimated or obtained from the literature, collateral experiments, or numerical fits to experimental data. In any event, design-oriented solutions to the model equations can be obtained without recourse to equipment-specific fitting parameters. Thus translation of scale from laboratory apparatus to production-scale equipment is possible. [Pg.200]

Both reactions are governed by specific parameters, which will be discussed briefly (1) hydrolysis of sodium silicate ... [Pg.16]

Many reviews covering several aspects of these topics have appeared in the recent years [1-7]. The purpose of this contribution is to focus on the major common features of the DNA-binding reactions of a now wide variety of complexes. The aim is to identify the specific parameters of each step of the overall platination reactions in order to design sequence-selective drugs. [Pg.224]

AC impedance spectra provide a large amount of information about the electrochemical system being investigated. However, the analysis of AC impedance spectra and the correlation of AC impedance spectra with a specific parameter are still not fully understood. For example, for electrochemical reactions under load (or with a certain reaction rate), how the charge-transfer resistance relates to the reaction rate is not clear. More work is needed to deduce electrochemical reaction parameters from these spectra. In a later part of this book, impedance derived from reaction mechanisms and its correlation with electric circuit components will be discussed. [Pg.29]

Other. Most drug substances used to manufacture dosage forms are solids. It is therefore necessary to consider other properties that may affect the bioavailability with the possibility of eliciting adverse reactions. These parameters, which should be adequately addressed both in the specifications and in the characterization/structure elucidation section, include the nature and extent of solvation, the possibility of different polymorphs, and particle size. [Pg.202]

The implications of the versatile reaction mechanisms depicted in Figs. 7-1 to 7-4 are profound with respect to the complete understanding and hence to the kinetic modeling of AOPs. Despite the complexity of these photo-initiated reactions, it is possible to model AOPs with sufficient precision if all the rate constants of OH radical reactions involved and those of all other elementary reactions are known (Crittenden et al., 1999). Most importantly, the structures and the concentrations of all intermediary reaction products must be known. In addition, photoreactor specific parameters have to be included, such as the incident photon flow d>p and the dimensions of the irradiated volume. This task can be achieved for example... [Pg.191]

The general difficulties in design and scale-up of bubble column reactors concern reaction specific data, such as solubilities and kinetic parameters as well as hydrodynamic properties. The paper critically reviews correlations and new results which are applicable in estimation of hydrodynamic parameters of two-phase and three-phase (slurry) bubble column reactors. [Pg.213]

It would be of interest to employ results like those in the preceding section to ascertain the applicability of the steady-state approximation in specific flames. This has been done by different investigators, often with conflicting conclusions. The primary reason for the differences is uncertainty in values of reaction-rate parameters. Key specific reaction-rate constants sometimes are uncertain by an order of magnitude at representative flame temperatures. Better rate-constant data are needed to aid in the application of the methods discussed herein to specific flames. [Pg.177]

P3-19c reaction rate parameters (i.e., reaction order, specific reaction rate at... [Pg.359]

Equations (54-56) and Eq. (59) reveal three important features of the solution. First, since the system of Eqs. (54-56) is invariant with respect to i, the explicit contribution of i to i] is incorporated in the logarithmic term in Eq. (59). Second, the appearance of a term 2b n(jo/I) with twice the Tafel slope of the pure reaction is a universal result, not due to any specific parameter values, following only... [Pg.484]

We should clarify here that the above cited studies are largely exploratory and the role of each parameter in reaction specificity is currently unclear. They show, however, the need for a fundamental understanding of molecular and electronic surface interactions that determine electrocatalytic as well as catalytic specificity. Thus, adsorption isotherms, surface states, molecular configurations, electronic distributions, dipole formation, and bond hybridization should be explored for well-characterized catalysts and model reactions in the presence and in the absence of an electric field. [Pg.283]

Specifying a relevant network of reactions and regulatory interactions requires at least qualitative kinetic information, but this specification establishes only the skeleton of the model. While certain qualitative results that are independent of specific parameter values can be obtained by mathematical analysis at this stage, more detailed quantitative predictions require that appropriate rate laws be specified for the reactions of the system. [Pg.113]


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See also in sourсe #XX -- [ Pg.162 ]




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Specific reaction parameters approximation

Specific reaction parameters, SRP

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