Big Chemical Encyclopedia

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

Articles Figures Tables About

Generation of Kinetic Data

Physical and chemical properties of the feedstock and product samples were obtained with the following standard methods API Gravity, ASTM D-287 kinematic viscosity, ASTM D-7042 (Stabinger SVM 3000 Viscometer) total sulfur, ASTM D-4294 total carbon, hydrogen, and nitrogen, ASTM D-5291 insolubles in nC, ASTM D-3279 metals (Ni and V), ASTM D-5863 (atomic adsorption) and yield of VR (538°C+), ASTM D-1160 distillation. [Pg.275]

FIGURE 8.4 Profiles of metals and sulfur content in product during time-on-stream. ( ) Ni + V, ( ) S (o) check-back experiment Tj = 380°C, 400°C, 420°C. [Pg.276]


Chapter 8 is dedicated to the modeling of heavy oil upgrading via hydroprocessing. Experimental studies for generation of kinetic data, catalyst deactivation, and long-term stability test are explained. Mass and heat balance equations are provided for the reactor modeling for steady-state and dynamic behavior. Simulations of bench-scale reactor and commercial reactor for different situations are also reported. [Pg.548]

The account of the formal derivation of kinetic expressions for the reactions of solids given in Sect. 3 first discusses those types of behaviour which usually generate three-dimensional nuclei. Such product particles may often be directly observed. Quantitative measurements of rates of nucleation and growth may even be possible, thus providing valuable supplementary evidence for the analysis of kinetic data. Thereafter, attention is directed to expressions based on the existence of diffuse nuclei or involving diffusion control such nuclei are not susceptible to quantitative... [Pg.48]

The stopped-flow method generates ordinary kinetic data, presenting values of the property Y, as a function of time. At one time, values were read from a Polaroid photograph of the oscilloscope, but nowadays computer acquisition, presentation, and... [Pg.254]

If chain transfer of the radical center to a previously formed polymer molecule is followed ultimately by termination through coupling with another similarly transferred center, the net result of these two processes is the combination of a pair of previously independent polymer molecules. T. G. Fox (private communication of results as yet unpublished) has suggested this mechanism as one which may give rise to network structures in the polymerization of monovinyl compounds. His preliminary analysis of kinetic data indicates that proliferous polymerization of methyl acrylate may be triggered by networks thus generated. [Pg.385]

Graphical Approach to the Analysis of Batteries of Stirred Tank Reactors Operating at Steady State. Even in reaction systems where it is not possible to determine the algebraic form of the reaction rate expression, it is often possible to obtain kinetic data that permit one to express graphically the rate as a function of the concentration of one reactant. Laboratory scale CSTR s are particularly appropriate for generating this type of kinetic data for complex reaction... [Pg.281]

Secondary phases predicted by thermochemical models may not form in weathered ash materials due to kinetic constraints or non-equilibrium conditions. It is therefore incorrect to assume that equilibrium concentrations of elements predicted by geochemical models always represent maximum leachate concentrations that will be generated from the wastes, as stated by Rai et al. (1987a, b 1988) and often repeated by other authors. In weathering systems, kinetic constraints commonly prevent the precipitation of the most stable solid phase for many elements, leading to increasing concentrations of these elements in natural solutions and precipitation of metastable amorphous phases. Over time, the metastable phases convert to thermodynamically stable phases by a process explained by the Guy-Lussac-Ostwald (GLO) step rule, also known as Ostwald ripening (Steefel Van Cappellen 1990). The importance of time (i.e., kinetics) is often overlooked due to a lack of kinetic data for mineral dissolution/... [Pg.650]

An isothermal, plug flow, fixed bed reforming pilot plant (shown in Fig. 14) was used to generate the kinetic data. The reactor was U shaped and contained roughly 70 ml of catalyst. Five sample taps were spaced along the reactor length to determine compositions over a wide range of catalyst contact times. The reactor assembly was immersed in a fluidized sand bath to maintain isothermal conditions. [Pg.226]

Pump-probe technique A flash photolysis technique in which the light beam (probe) used for spectral analysis is generated from a portion of the excitation (pump) beam. A time delay in the latter allows the obtention of kinetic data. [Pg.335]

The methods of generation of the radical and of analysis of different types of kinetic data have been referred to. Optical detection of species was made, primarily of the parent dimer itself or of certain products referred to later. [Pg.206]

Experimentally measured values reported in the literature provide the primary source of kinetic data for the modeller. However, this information may be widely scattered and of variable quality. This has generated a need for bibliographies, reviews and critical assessments of the reported data to aid scientists and technologists who are not expert in chemical kinetics. In this section we review the main limitations of the primary data indicating how the need for compilation and critical evaluation has arisen. [Pg.238]

Another way of generating reaction schemes consisting of global reactions is to fit the parameters of one or a few global reactions to some kind of kinetic data. The data may come from experiments or detailed chemical kinetic simulations. Fitting a small kinetic scheme requires the optimization of the parameters of a system of ordinary differential equations. If the reaction scheme consists of elementary reactions, and the parameters are optimized only within the physically feasible boundaries, the approach of the GRI mechanism (Section 4.3.7) is reproduced. The fitting of parameters in small schemes is described in the following sections. [Pg.403]

The first stage in the formulation of a repro-model is the generation of suitable data. Usually, several thousand typical data points are considered and a detailed model is used for the calculation of the concentrations as a function of time. The evaluation of a large number of data points requires quite intensive computation, since, large sets of odes must be solved for all conditions. However, this effort has to be expended only once, and when the data have been fitted to polynomials, the repeated kinetic calculations, which are generally carried out during every CFD calculation, are avoided. [Pg.412]

Current-generating Measurement of kinetic data Electrochemical energy storage and... [Pg.7]

Fig. 9. The variation of the quantities gO, K) and g(j) with j for the species Red undergoing a simple kinetically uncomplicated electrode reaction Red Ox + e. The parameters used in the generation of the data are as in Fig. 8 (see text). Fig. 9. The variation of the quantities gO, K) and g(j) with j for the species Red undergoing a simple kinetically uncomplicated electrode reaction Red Ox + e. The parameters used in the generation of the data are as in Fig. 8 (see text).

See other pages where Generation of Kinetic Data is mentioned: [Pg.443]    [Pg.356]    [Pg.55]    [Pg.137]    [Pg.274]    [Pg.443]    [Pg.356]    [Pg.55]    [Pg.137]    [Pg.274]    [Pg.117]    [Pg.118]    [Pg.118]    [Pg.509]    [Pg.84]    [Pg.17]    [Pg.56]    [Pg.8]    [Pg.17]    [Pg.154]    [Pg.5]    [Pg.276]    [Pg.375]    [Pg.113]    [Pg.192]    [Pg.158]    [Pg.56]    [Pg.627]    [Pg.158]    [Pg.877]    [Pg.61]    [Pg.310]    [Pg.425]    [Pg.342]    [Pg.158]    [Pg.92]    [Pg.57]    [Pg.290]    [Pg.192]    [Pg.243]    [Pg.246]   


SEARCH



Data generation

© 2024 chempedia.info