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Numerical Analysis of Experimental Data

This example shows that mixed-mode oscillations, while arising from a torus attractor that bifurcates to a fractal torus, give rise to chaos via the familiar period-doubling cascade in which the period becomes infinite and the chaotic orbit consists of an infinite number of unstable periodic orbits. Mixedmode oscillations have been found experimentally in the Belousov-Zhabotin-skii (BZ) reaction 2.84 and other chemical oscillators and in electrochemical systems, as well. Studies of a three-variable autocatalator model have also provided insights into the relationship between period-doubling and mixedmode sequences. Whereas experiments on the peroxidase-oxidase reaction have not been carried out to determine whether the route to chaos exemplified by the DOP model occurs experimentally, the DOP simulations exhibit a route to chaos that is probably widespread in the realm of nonlinear systems and is, therefore, quite possible in the peroxidase reaction, as well. [Pg.259]


Equation (48) e ees with experimental results in some circumstances. This does not mean the mechanism is necessarily correct. Other mechanisms may be compatible with the experimental data and this mechanism may not be compatible with experiment if the physical conditions (temperature and pressure etc.) are changed. Edelson and Allara [15] discuss this point with reference to the application of the steady state approximation to propane pyrolysis. It must be remembered that a laboratory study is often confined to a narrow range of conditions, whereas an industrial reactor often has to accommodate large changes in concentrations, temperature and pressure. Thus, a successful kinetic model must allow for these conditions even if the chemistry it portrays is not strictly correct. One major problem with any kinetic model, whatever its degree of reality, is the evaluation of the rate cofficients (or model parameters). This requires careful numerical analysis of experimental data it is particularly important to identify those parameters to which the model predictions are most sensitive. [Pg.124]

Computational techniques are centrally important at every stage of investigation of nonlinear dynamical systems. We have reviewed the main theoretical and computational tools used in studying these problems among these are bifurcation and stability analysis, numerical techniques for the solution of ordinary differential equations and partial differential equations, continuation methods, coupled lattice and cellular automata methods for the simulation of spatiotemporal phenomena, geometric representations of phase space attractors, and the numerical analysis of experimental data through the reconstruction of phase portraits, including the calculation of correlation dimensions and Lyapunov exponents from the data. [Pg.265]

The success of SECM methodologies in providing quantitative information on the kinetics of interfacial processes relies on the availability of accurate theoretical models for mass transport and coupled kinetics, to allow the analysis of experimental data. The geometry of SECM is not conducive to exact analytical solution and hence a number of semiana-lytical [40,41], and numerical [8,10,42 46], methods have been introduced for a variety of problems. [Pg.296]

An alternative scheme, proposed by Garside et al. (16,17), uses the dynamic desupersaturation data from a batch crystallization experiment. After formulating a solute mass balance, where mass deposition due to nucleation was negligible, expressions are derived to calculate g and kg in Equation 3 explicitly. Estimates of the first and second derivatives of the transient desupersaturation curve at time zero are required. The disadvantages of this scheme are that numerical differentiation of experimental data is quite inaccurate due to measurement noise, the nucleation parameters are not estimated, and the analysis is invalid if nucleation rates are significant. Other drawbacks of both methods are that they are limited to specific model formulations, i.e., growth and nucleation rate forms and crystallizer configurations. [Pg.104]

Until recently the application of computers in chemistry was restricted to two fields. First, there were numerical calculations as for the analysis of experimental data and in quantum mechanical computations, and second, computers were used for documentation and information retrieval. [Pg.95]

The proper analysis of experimental data requires careful consideration of the numerical techniques used. Real data are subject to experimental error which can have an effect on results derived from the analysis. Often, this analysis involves fitting a curve to experimental data over the whole range or over part of the range in which experimental observations have been made. When thermodynamic data are involved, the relationship between the independent and dependent variable is usually not known. Then, arbitrary functions such as polynomials in the independent variable are often used in the data analysis. This type of data analysis requires consideration of the level of error in both variables, and of the effects of the error on derived results. [Pg.595]

Numerical integration techniques are easily applied in the analysis of experimental data which are acquired digitally. Thus, values of the electrical current which are obtained as a function of time for a fixed interval between observations are easily converted to electrical charge by numerical integration. [Pg.614]

Before discussing in detail the numerical results of our computational work, we describe the theoretical and computational context of the present calculations apart from deficiencies of models employed in the analysis of experimental data, we must be aware of the limitations of both theoretical models and the computational aspects. Regarding theory, even a single helium atom is unpredictable [14] purely mathematically from an initial point of two electrons, two neutrons and two protons. Accepting a narrower point of view neglecting internal nuclear structure, we have applied for our purpose well established software, specifically Dalton in a recent release 2.0 [9], that implements numerical calculations to solve approximately Schrodinger s temporally independent equation, thus involving wave mechanics rather than quantum... [Pg.347]

The tight-binding (TB) approximation is commonly used for theoretical consideration of the electronic structure of carbon nanotubes [1]. But it is desired to have a simpler qualitative model to predict physical properties of nanotubes without bulky numerical calculations and to assist in analysis of experimental data. For example, in [2] the free-electron (FE) model has been used. The aim of this work is to improve this model by taking into account the finite thickness of nanotube conducting layer. We compare our FE approximation with the commonly used TB approach to determine its area of application. [Pg.186]

Sada et.al.(10,15) considered the case where the reaction was finite and presented numerical solutions(An approximate solution for this case was obtained previously(4) j.Sada et.al.(11) considered simultaneous absorption of two gases and presented numerical analysis and experimental data.They(16) have interpreted also their experimental results on dilute sulphur dioxide absorption into aqueous slurries of sparingly soluble fine rectant particles in terms of a "two-reaction plane" model.Sada et.al.(17, 18) considered also other interesting examples and proposed a model on the basis of above discussed theory as well as incorporating the possible solid surface reaction.In this case,the... [Pg.880]

The Grain Boundary Impedance of Random Microstructures, Numerical Simulations and Implications for the Analysis of Experimental Data,... [Pg.552]

At this point, several considerations have to be taken into account. First, two techniques, SFG and PFG NMR, are used to get those measurements. Both use the same principle but McCall, et al. did some of their experiments at the lower limit of measurable diffusivity using SFG NMR with increased uncertainties in their measurements. Second, in the case of PDMS melts, the effect of polydispersity upon the echo attenuation and its interpretation is repeatedly pointed out but only Garrido, et al. explicitly included its effect in the numerical analysis of the data. In this case, no significant effect of polydispersity was detected, at least within the range of echo attenuations observed. Third, as mentioned earlier, free volume effects cannot be ignored in explaining diffusion in polymer melts when their M is smaller than Af. However, for PDMS chains with Af 2 3,000 g-mol the contribution of the third term in Eq. (5) to free volume fraction would be relatively small (less than 1J) at the experimental conditions at which the diffusion measurements have been performed (150 K above its T 1 35,36... [Pg.361]

The comparison of the experimental data with numerical simulations of high spatial resolution shows a remarkable agreement regarding the symmetry and tip dynamics of pairs of spiral waves. The reason why in most experiments pairs of counter-rotating spirals appear is found in the experimental procedure that normally generates two open ends of a wave which both curl up to a pair of spirals. An analysis of experimental data showed that the spirals evolve independently of each other without any synchronisation of their motion. The... [Pg.89]

Numerical resolution of mass-transport equations, along with Laplace formulation of the electrical properties of the SECCM system, is an efficient and reliable strategy for the characterization of SECCM mass transport, technique optimization, and the analysis of experimental data with the aim of extracting quantitative information. This is an indispensable tool not only for detailed examination of experimental data but also for developing novel experiments and exploiting new phenomena that can be examined with SECCM. [Pg.668]

Predicting the solvent or density dependence of rate constants by equation (A3.6.29) or equation (A3.6.31) requires the same ingredients as the calculation of TST rate constants plus an estimate of and a suitable model for the friction coefficient y and its density dependence. While in the framework of molecular dynamics simulations it may be worthwhile to numerically calculate friction coefficients from the average of the relevant time correlation fiinctions, for practical purposes in the analysis of kinetic data it is much more convenient and instructive to use experimentally detemiined macroscopic solvent parameters. [Pg.849]

In Spite of the existence of numerous experimental and theoretical investigations, a number of principal problems related to micro-fluid hydrodynamics are not well-studied. There are contradictory data on the drag in micro-channels, transition from laminar to turbulent flow, etc. That leads to difficulties in understanding the essence of this phenomenon and is a basis for questionable discoveries of special microeffects (Duncan and Peterson 1994 Ho and Tai 1998 Plam 2000 Herwig 2000 Herwig and Hausner 2003 Gad-el-Hak 2003). The latter were revealed by comparison of experimental data with predictions of a conventional theory based on the Navier-Stokes equations. The discrepancy between these data was interpreted as a display of new effects of flow in micro-channels. It should be noted that actual conditions of several experiments were often not identical to conditions that were used in the theoretical models. For this reason, the analysis of sources of disparity between the theory and experiment is of significance. [Pg.104]

The data from the method validation data should be analyzed as the data are obtained and processed to ensure a smooth flow of information. If an experimental error is detected, it should be resolved as soon as possible to reduce any impact it may have on later experiments. Analysis of the data includes visual examination of the numerical values of the data and chromatograms followed by statistical treatment of the data if required. [Pg.737]

I. Bruker, C. Miaw, A. Hasson, and G. Balch, Numerical Analysis of the Temperature Profile in the Melt Converying Section of a Single Screw Extruder Comparison with Experimental Data, Polym. Eng. Sci., 27, 504 (1987). [Pg.315]


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