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One-level decomposition

Coarse-Filtered One-Level Decomposition The coarse-filtered (low-pass)... [Pg.148]

Detail-Filtered One-Level Decomposition The detail-filtered (high-pass) coefficients of the first resolution level represent a new type of descriptor that reveals special aspects of data, like trends, breakdown points, and discontinuities in higher derivatives. It is useful as alternative molecular representation for neural networks in classification and prediction tasks (Figure 5.20). [Pg.148]

Coarse-filtered WLT at resolution level j = 1 (one-level decomposition)... [Pg.161]

Data compression is another application of WT that has shown remarkable results (Artursson and Holmberg 2002). The mathematical treatment for data compression by WT is similar to that for denoising and smoothing (fetter et al. 2000). Chemical data is treated with WT and transformed to the scale-time domain where its spectral content is reduced by elinunating coefficients belonging to high frequency content. Compression with this teclmique is highly efficient since a one level decomposition and... [Pg.154]

Comparison of the two elementary processes (2) and (3) shows the latter to be the most endothermic one. Indeed, decomposition of N2O yielding NO and N entails the rupture of the N=N bond, which requires 85 kcal. mole (3.6 e.v. molecule ) whereas for N2O decomposition into Na and 0, the breaking of the NO bond requires only 38 kcal. mole (1.6 e.v. molecule 0-This explains that thermally, in the absence of radiation, reaction (2) is always considerably favored, compared to reaction (3). Under irradiation, however, a great number of excess free carriers are produced in the conduction and valency bands these carriers tend to recombine. In this respect the adsorbed N2O molecule may behave like a recombination center. This phenomenon can be accounted for by considering the adsorbed N2O molecule to be an acceptor level. Under this hypothesis, the N2O chemisorption results from the capture, by the weakly adsorbed molecule, of an electron from the conduction band. At the moment of recombination with a positive hole from the valency band, a variable amount of energy can be recovered, depending on the position of the level constituted by the adsorbed N2O molecule. For the silica and alumina we have utilized, the width of the forbidden region is about 10 e.v. process (3) which only requires 3.6 e.v. may thus become possible. [Pg.127]

Figure 10.16. Filtered approximation of Y through wavelet denoising using hard-thresholding with one level of decomposition (left) and two levels of decomposition. Figure 10.16. Filtered approximation of Y through wavelet denoising using hard-thresholding with one level of decomposition (left) and two levels of decomposition.
Besides the generators described above there are X-ray sources based on radioactive materials to provide the excitation of the sample. The advantage of using these materials is that an isotope can be selected to provide a mono-energetic beam of radiation that is optimized for the specific application. One method consists to select a radionuclide that is transformed by internal electron capture (lEC). This mode of decomposition corresponds to the transition of one level-K electron into the nucleus of the atom. For a nuclide X, the phenomenon is summarized as follows ... [Pg.269]

The following conditions are stipulated the catalyst decomposition rate constant must be one hour or greater the residence time of the continuous reactor must be sufficient to decompose the catalyst to at least 50% of the feed level the catalyst concentration must be greater than or equal to 0.002 x Q, where the residence time, is expressed in hours. An upper limit on the rate of radical formation was also noted that is, when the rate of radical formation is greater than the addition rate of the primary radicals to the monomers, initiation efficiency is reduced by the recombination of primary radicals. [Pg.280]

Coke formation on these catalysts occurs mainly via methane decomposition. Deactivation as a function of coke content (see Fig. 3 for Pt/ y-AljO,) seems to involve two processes, i e, a slow initial one caused by coke formed from methane on Pt that is non reactive towards CO2 (see Table 3) In parallel, carbon also accumulates on the support and given the ratio between the support surface and metal surface area at a certain level begins to physically block Pt deactivating the catalyst rapidly. The coke deposited on the support very close to the Pt- support interface could be playing an important role in this process. [Pg.470]

The SiC diluent did not contribute to the N2O decomposition at the reaction temperatures studied. Prior to each run, the catalyst was subjected to calcination by heating the catalyst in He at 30 K/min to 923 K and maintaining this temperature for one hour. Subsequently, the temperature was decreased to the desired value and the feed mixture was passed over the bed. Temperature and feed composition were varied in a random order in the experiments. Generally, 40 to 50 min after a change of conditions the conversion levels were constant and considered as the steady-state. At least five analyses were averaged for a data point. [Pg.643]

One of the interesting examples is the metal molecular cluster, like Os3(CO)i2 in which during decomposition a dramatic change in the metal core-level BE occurs... [Pg.81]

When analysing the previous table, it shows the ambiguity of NFPA reactivity codes vis-a-vis instability. It is not so much an instability code but rather, like its name indicates, a code related to dangerous chemical reactions. Degrees 3 and 4 are the only ones that are more or less usable for defining an instability level, with the exception of ethylene oxide. So, even ethylene oxide s main hazard is not its explosive decomposition but its very violent polymerization caused by catalytic impurities (see chapter 6). [Pg.121]

At another level, certain KBS approaches provide the mechanisms for decomposing complex interpretation problems into a set of smaller, distributed and localized interpretations. Decomposition into smaller, more constrained interpretation problems is necessary to maintain the performance of any one interpreter and it makes it possible to apply different interpretation approaches to subparts of the problem. It is well recognized that scale-up is a problem for all of the interpretation approaches described. With increases in the number of input variables, potential output conclusions, complexity of subprocess interactions, and the spatial and temporal distribution of effects, the rapidity, accuracy, and resolution of interpretations can deteriorate dramatically. Furthermore, difficulties in construction, verification, and maintenance can prohibit successful implementation. [Pg.72]


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See also in sourсe #XX -- [ Pg.148 ]




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