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Modeling efficiency

Recently the applicability of the APM has been reinvestigated by Staveley and his co-workers17 18 and by Knobler et al.1B in relation to the latest experimental data available on simple mixtures, with rather discouraging results. It actually seems to us that the analysis of these authors neither validates nor invalidates the APM itself but rather shows how difficult it is to use the model efficiently for practical calculations on account of points (a), (b), and (c) listed above. [Pg.120]

For fuzzy virtual screening purposes, highly active molecules with different scaffolds are combined into an MTree model. By combining the information of remotely related actives into a single model, efficient database searches with molecule ensembles are possible. [Pg.95]

FIGURE 3.23 Tradeoff between model efficiency and level of detail. [Pg.95]

Christiansen, T.R. Modeling Efficiency and Effectiveness of Coordination in Engineering Design Teams. PhD thesis, Stanford University (1993)... [Pg.823]

A model for predicting the efficiency of dualflow-type trays has been reported and is mechanistic in character. A large efficiency database, provided by Fractionation Research, Inc. (FRl), was used in constracting the model. Efficiency data for counterflow baffle tray columns are sparse, and the only model available is based largely on a heat transfer database, using the appropriate analogies. [Pg.1065]

There are also situations where two of the modes of the three-way array can be expressed as qualitative variables in a two-way ANOVA and where the response measured is some continuous (spectral, chromatogram, histogram or otherwise) variable. Calling the ANOVA factors treatment A and treatment B a (Treatment x Treatment x Variable) array is made, see Figure 10.5. An example for particle size distribution in peat slurries was explained in Chapters 7 and 8. The two-way ANOVA can become a three-way ANOVA in treatments A, B and C, leading to a four-way array etc. Having three factors and only one response per experiment will lead to a three-way structure and examples will be given on how these can be modeled efficiently even when the factors are continuous. [Pg.258]

Even though this comprehensive model for the general case of high solids loading industrial crystallization remains unachieved, the success of modeling the limited cases of low concentration precipitation (to which I ve previously referred) suggests that this approach should be quite successful when advances in computing power and model efficiency make the extension to conventional crystallization possible. [Pg.197]

Production planning models efficient allocation of manufacturing resources over a period of several months to meet demand... [Pg.2009]

In later work, Lattimer et al. identified eight oligomeric series in a commercial version of poly-TMDQ by using the LC/FD-MS combination. Components of f-octylphenol/formaldehyde resins were also characterized using this method. In a series of studies, ozonation products of several p-phenylenediamine compoimds (rubber antiozonants) were separated by LC and identified by using FD-MS. In another study, model "efficient vulcanization" products were separated by colunm chromatography and characterized by FD-MS. "... [Pg.268]

Fig. 12 Comparison of FCI model efficiencies for stoichiometric Iron-alximlna thermite. Fig. 12 Comparison of FCI model efficiencies for stoichiometric Iron-alximlna thermite.
Figure 17.1.11 Coulometric efficiencies for a data set obtained with a beveled 33- tm electrode ( ) compared to data obtained with a 5-pm electrode ( ) for release of catechol measured from a range of vesicle sizes. This is compared to the theoretical coulometric efficiencies for these electrode dimensions calculated with the conditions outlined in Figure 17.1.5 and with the model discussed in the text (dashed lines). These are compared to each set of experimental data, which are shown with best-fit equations (thick lines). The equations for all lines, and their correlation coefficients, are given with the symbols for experimental data sets and for the modeled efficiencies with that for the 5- jm electrode to the left and that for the 33-pm electrode to the right. Reproduced with permission from reference (80). (for colour version see colour section at the end of the book). Figure 17.1.11 Coulometric efficiencies for a data set obtained with a beveled 33- tm electrode ( ) compared to data obtained with a 5-pm electrode ( ) for release of catechol measured from a range of vesicle sizes. This is compared to the theoretical coulometric efficiencies for these electrode dimensions calculated with the conditions outlined in Figure 17.1.5 and with the model discussed in the text (dashed lines). These are compared to each set of experimental data, which are shown with best-fit equations (thick lines). The equations for all lines, and their correlation coefficients, are given with the symbols for experimental data sets and for the modeled efficiencies with that for the 5- jm electrode to the left and that for the 33-pm electrode to the right. Reproduced with permission from reference (80). (for colour version see colour section at the end of the book).
Continuum Solvation Models Efficient Way to Account for Solvent Effects in Vibrational Spectroscopy... [Pg.309]

In our works we have modeled efficient catalytic systems (ML + L (M = Ni, Fe, are crown ethers or quaternary ammonium salts) for ethylbenzene oxidation to PEH, that was based on the established (for Ni complexes) and hypothetical (for Fe complexes) mechanisms of formation of catalytically active species and their operation. 2 Selectivity (Spgjj), conversion, and yield of PEH in ethylbenzene oxidation catalyzed by these systems were substantially higher than those observed with conventional catalysts of ethylbenzene oxidation to PEH. - ... [Pg.76]

RE technique can create 3D model efficiently for new solid modeling which can be often redesigned. [Pg.1596]


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