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Model parameter values, obtaining

In this study, four other kinetic models with or without water inhibition from references [11,13,20,25] plus the CAER model are used to lit the experimental results of the 15% Co/Si02 catalyst. The kinetic parameter values obtained based on the same analysis method along with MARR values are listed in Table 3.2. [Pg.37]

Table I lists the values of the rate coefficients used to simulate the transient response experiments shown in Figs. 3 through 8. These values were obtained in the following manner (29). Starting from a set of initial guesses, the values of k were varied systematically to obtain a fit between the predicted product responses and those obtained from experiments in which H2 was added suddenly to a flow of NO. These experiments while not described here were identical to that presented in Fig. 9, with the exception that only l NO was used. Because of the large number of parameters in the model, only a rough agreement could be achieved between experiment and theory even after 500 iterations of the optimization routine (30). The parameter values obtained at this point were now used to calculate the responses expected during the reduction of adsorbed NO. These computations produced responses similar to those observed experimentally (i.e., Fig. 3) but the appearance of the product peaks in time did not coincide with those observed. To correct for this, the values of kg, ky, and kg were adjusted in an empirical manner. Table I lists the values of the rate coefficients used to simulate the transient response experiments shown in Figs. 3 through 8. These values were obtained in the following manner (29). Starting from a set of initial guesses, the values of k were varied systematically to obtain a fit between the predicted product responses and those obtained from experiments in which H2 was added suddenly to a flow of NO. These experiments while not described here were identical to that presented in Fig. 9, with the exception that only l NO was used. Because of the large number of parameters in the model, only a rough agreement could be achieved between experiment and theory even after 500 iterations of the optimization routine (30). The parameter values obtained at this point were now used to calculate the responses expected during the reduction of adsorbed NO. These computations produced responses similar to those observed experimentally (i.e., Fig. 3) but the appearance of the product peaks in time did not coincide with those observed. To correct for this, the values of kg, ky, and kg were adjusted in an empirical manner.
Table 2.4 shows the SAS NLIN specifications and the computer output. You can choose one of the four iterative methods modified Gauss-Newton, Marquardt, gradient or steepest-descent, and multivariate secant or false position method (SAS, 1985). The Gauss-Newton iterative methods regress the residuals onto the partial derivatives of the model with respect to the parameters until the iterations converge. You also have to specify the model and starting values of the parameters to be estimated. It is optional to provide the partial derivatives of the model with respect to each parameter, b. Figure 2.9 shows the reaction rate versus substrate concentration curves predicted from the Michaelis-Menten equation with parameter values obtained by four different... [Pg.26]

Model parameters were obtained by fitting dynamic DSC scans at 10 K min-1 for a formulation with I0 / M0 = 0.043. The following set of values was obtained ... [Pg.173]

The latter free energy can be represented as a surface integral over the solvent accessible surface of the molecule on the basis of a local free energy surface density (FESD) p. This surface density function is represented in terms of a three-dimensional scalar field which is comprised of a sum of atomic increment functions to describe lipophilicity in the molecular environment.The empirical model parameters are obtained by a least squares procedure with experimental log P values as reference data. It is found that the procedure works not only for the prediction of unknown partition coefficients but also for the localization and quantification of the contribution of arbitrary fragments to this quantity. In addition, the... [Pg.230]

Assumptions are used to simplify the biological system to a mathematically and computationally tractable level. For any model the following questions must always be asked What are the assumptions and Flow valid are they Moreover, a model is only as good as the parameters used. As published PBPK parameters are not always consistent [75], parameter values obtained from the literature must be used with care. Relatively recently PBPK model parameters have been compiled [76]. [Pg.49]

The deconvolution methods are multi-wavelength procedures which can be classified with regard to the selection procedure of reference spectra. These spectra can be chosen from specific compounds (Maier, 1981), from independent spectra of real samples (Thomas et al., 1993), statistically selected (Gallot and Thomas, 1993) or from a mixed choice of spectra of specific compounds and of real samples. Reference spectra are not universal recently, according to the complexity of the composition of wastewater, SECOMAM has developed UVPro software based on advanced UV spectral deconvolution (Patent 00402038-4, 17 July 2000) which allows creating dedicated models and determination of reference spectra from a set of studied water and wastewater UV spectra an automatic calibration step is carried using parameters values obtained by standard or reference method. Deconvolution is used in order to find a linear relation between measured and UV estimated values for any parameter. [Pg.92]

Instrument calibration or models creation (Recalibration module), this module is used when the existing models are not fitting well with the sample composition. In this case, it is necessary to create a new model on the base of a set of relevant spectra (minimum of 20 spectra). The parameters values obtained by laboratory methods (COD, TOC, BOD...) are included in the data base in order to found the more suitable model. [Pg.95]

The experimental data in Figures 3 and 4 show the relationship of F, the fraction of total HOC that is either solubilized or dissolved, to the dose of applied surfactant. The model results are calculated with the approach already outlined (7), by using parameter values obtained from independent experiments (viz. S/Scme = 0.62 for phenanthrene and C8PE95, and 0.63 for C12E4 (9) / = 0 015 = 5.7 X HP6 mol/g for C8PE95 (10) < surf for C12E4 from... [Pg.350]

Figures 3 and 4 show good agreement between the experimental data and the solubilization values predicted by the model. Apparently the more important physical and chemical processes can be characterized with parameter values obtained from independent tests in aqueous and soil-aqueous systems. In addition, gross solubilization data alone can be used in an inverse procedure to calibrate the ratio between Kdcmc and (12). Figures 3 and 4 show good agreement between the experimental data and the solubilization values predicted by the model. Apparently the more important physical and chemical processes can be characterized with parameter values obtained from independent tests in aqueous and soil-aqueous systems. In addition, gross solubilization data alone can be used in an inverse procedure to calibrate the ratio between Kdcmc and (12).
These results agree well with those of Lucy et al. [62] obtained in a few specific experimental cases. Band profiles were recorded at increasing sample sizes for a series of compounds, and fitted to the Thomas model. The values obtained for the limit retention factor, fcg, and the column saturation capacity were nearly independent of the sample size, while the kinetic parameter was concentration dependent (Figure 14.16). [Pg.686]

In the triple layer model, values for the intrinsic protonation and dissociation constants, as well as values for tlie intrinsic surface complexation constants for the background electrolyte, can be obtained from hnear, double, or electrokmetic extrapolations to zero surface charge and zero and infinite electrolyte concentration. Values of intrinsic protonation-dissociation constants and intrinsic surface complexation constants for background electrolytes obtamed for the triple layer model using the various extrapolations are compiled in Goldberg (1992). Use of graphical extrapolation methods has been criticized because the triple layer parameter values obtained are not unique (Koopal et al., 1987). [Pg.235]

To model the distribution of pain relief scores and remedication times, subject-specific random effect models are developed. Let the vector of pain relief scores for an individual be Y = (Yi, Y2,..., Y r). At time t the pain relief score is denoted by Y, and the time at which an individual remedicates is denoted by the variable T. The PD model parameter estimates are obtained by maximum likelihood, which estimates the most probable model parameter values for the observed data. P[T, Y] denotes the likelihood of an individual s data, and it is expressed by the following equation ... [Pg.661]

The fitted parameters may or may not be of intrinsic interest. It is important to remember that the parameter values obtained depend on the specific Heff model, the parameters allowed to vary in the fit, the fixed values chosen for parameters not allowed to vary, and the specific subset of spectral data fitted. Generation of multidigit molecular constants should not normally be the primary objective nor the stopping point of a spectroscopic investigation. [Pg.255]

To verify the model parameters or obtain the parameter values for an existing actuator, a frequency sweep to measure the DE s electrical impedance can be done. [Pg.728]


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