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Hybrid modelling concentration

Prindle and Ray (ZB.) have recently analyzed the same styrene data using a hybrid model consisting of the micellar nucleation mechanism above the CMC and of the homogeneous nucleation and coagulation mechanism below the CMC. Their simulations show a much steeper rise in the particle number concentration precisely at the CMC than predicted by EPM. Their hybrid model does not appear to predict that the particle concentration levels off at high surfactant concentrations. [Pg.375]

Employing the additivity approximation, we find dielectric response of a reorienting single dipole (of a water molecule) in an intermolecular potential well. The corresponding complex permittivity jip is found in terms of the hybrid model described in Section IV. The ionic complex permittivity A on is calculated for the above-mentioned types of one-dimensional and spatial motions of the charged particles. The effect of ions is found for low concentrated NaCl and KC1 aqueous solutions in terms of the resulting complex permittivity e p + Ae on. The calculations are made for long (Tjon x) and rather short (xion = x) ionic lifetimes. [Pg.81]

If the electrolyte concentration Cm varies, the wideband spectra are controlled only by one parameter (x) of the hybrid model. Other parameters of this model—the normalized well depth u, the libration amplitude ft, and the p-correcting coefficient —can be set independent of Cm and therefore could be fit by comparison of the calculated and recorded [70, 71] spectra of water (see Table XVI). [Pg.282]

Note that in this specific model, desorption is neglected, and sites get regenerated upon adsorption, so the classic Langmuir blocking of sites is uncommon for MBE modeling. Furthermore, the diffusion-adsorption model for the terrace is only approximate since interactions between molecules are not accounted for. As a result, this hybrid model cannot handle nucleation between terraces, and applies only to small supersaturations or high temperatures [note that for high temperatures, one needs to include desorption in Eq. (2)] where the adatom concentration on terraces is relatively low. [Pg.22]

The hybrid model proposed by Zingmark et al. (26) is a straightforward way of incorporating Markov elements in an analysis of ordered categorical data. An inappropriate model—a bad descriptive model or a model with a bad predictive performance (see Ette et al. (34) Chapter 8 of this text)—would result if the correlated nature of the data is ignored and a proportional odds model is used to characterize the concentration-adverse effect relationship. Readers are referred to the article by Zingmark et al. (26) for a detailed description of the hybrid model. They also provide a NONMEM data set and control file for the implementation of the model. [Pg.696]

Fig. 5. Comparison of the concentration profiles obtained with the hybrid model for isothermal and isobaric runs performed at Tr = 308 K and at different partial hydrogen pressures p. ... Fig. 5. Comparison of the concentration profiles obtained with the hybrid model for isothermal and isobaric runs performed at Tr = 308 K and at different partial hydrogen pressures p. ...
Fuzzy clustering will be used to build a model of the net growth rate as a fimction of the substrate concentration Cg and biomass concentration Cx for the hybrid model of the bioreactor. Assume that an input-output data set has been created using all identification experiments and that the Pl-estimator data are available in the form of measurements. This means that input-output data are available of Cs and Cx and estimates of ju and n . The data set can be presented directly to the clustering algorithm. The initial number of clusters was ten. This number was reduced to three by the merging algorithm. The next step is to project the fuzzy partition matrix onto the cs and cx axis, so that parametric membership fimctions can be determined. This is shown in Fig. 30.9. [Pg.421]

The initial performance of the hybrid model for one of the validation sets, before optimization, is shown in Fig. 30.11. It can be seen that for this run, the concentration cp starts to decrease after about 160 hours, which is not possible. This is caused by anomalous behavior of k The production rate decreases after 160 hours, which results in a decrease in production of P. Because the amount of P in the reactor is diluted, the net result is a decrease in the concentration of P. The increase in 5 is caused by a decrease in the substrate consumption rate, which is a result of the decrease in m... [Pg.423]

The goal is to improve hybrid model performance with respect to the errors in the biomass concentration Cx, the substrate concentration cs and the product concentration cp. This will be done by using the measurements from the identification batch runs as a reference. The objective function is formulated according to ... [Pg.423]

To identify the fuzzy models for reaction rates and diffusion coefficient, input-output data are required. The inputs can be obtained from the simulation model. However, the ontputs Ri pi,p4,T), R2(PhPA,T), R ,iPi,P4,T) and >(7)) of the fuzzy models caimot be readily obtained. The outputs are therefore derived from observed behavior by Pl-estimation (van Lith et al., 2001). The reaction rates and diffusion coefficient can be estimated with the help of the mass balances of species of the hybrid model and the steady state profiles from the identification experiments. The estimators were tuned manually by comparing the concentration profiles with the reference values from the simulation model. [Pg.431]

Schematic representation of the hybrid model (TMP trans-membrane pressure Q feed flow rate Cq-. feed concentration of BSA solutions fp i pulse time f p operating time Jp(t) permeate flux decay). [Pg.585]

FIGURE 113 (a) The framework of bonds shown in the tube model of benzene are cr bonds (b) Each carbon is sp hybridized and has a 2p orbital perpendicular to the cr framework Overlap of the 2p orbitals generates a tt system encompass mg the entire ring (c) Electrostatic potential map of benzene The red area in the center corresponds to the region above and below the plane of the ring where the tt electrons are concentrated... [Pg.430]

Figures 1 a and 1 b represent the two-phase and the three-phase models respectively in the representative volume element of the composite. In the modified model three concentric spheres were considered with each phase maintaining a constant volume 4). The novel element in this model is the introduction of the third intermediate hybrid phase, lying between the two principal phases. Figures 1 a and 1 b represent the two-phase and the three-phase models respectively in the representative volume element of the composite. In the modified model three concentric spheres were considered with each phase maintaining a constant volume 4). The novel element in this model is the introduction of the third intermediate hybrid phase, lying between the two principal phases.
When there is more than one central atom in a molecule, we concentrate on each atom in turn and match the hybridization of each atom to the shape at that atom predicted by VSEPR. For example, in ethane, C2H6 (38), the two carbon atoms are both central atoms. According to the VSEPR model, the four electron pairs around each carbon atom take up a tetrahedral arrangement. This arrangement suggests sp hybridization of the carbon atoms, as shown in Fig. 3.14. Each... [Pg.232]

Usually, the buffer compartment is not accessible and, consequently, the absolute amount of X cannot be determined experimentally. For this reason, we will only focus our discussion on the plasma concentration Cp. It is important to know, however, that the time course of the contents in the two compartments is the sum of two exponentials, which have the same positive hybrid transfer constants a and p. The coefficients A and B, however, depend on the particular compartment. This statement can be generalized to mammillary systems with a large number of compartments that exchange with a central compartment. The solutions for each of n compartments in a mammillary model are sums of n exponential functions, having the same n positive hybrid transfer constants, but with n different coefficients for each particular compartment. (We will return to this property of linear compartmental systems during the discussion of multi-compartment models in Section 39.1.7.)... [Pg.480]

Fig. 39.13. (a) Semilogarithmic plot of the plasma concentration Cp (pg 1 ) versus time /. The straight line is fitted to the later part of the curve (slow P-phase) with the exception of points that fall below the quantitation limit. The intercept Bp of the extrapolated plasma concentration appears as a coefficient in the solution of the model. The slope is proportional to the hybrid transfer constant p, which is itself a function of the transfer constants of and ifcbpOf the model, (b) Semilogarithmic plot of the... [Pg.482]


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