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Scaling data representation

Data Representation. Transformations can be applied to the data so that they will more closely follow the normal distribution that is required for certain procedures or for removing (or lessening) unwanted influences. Certainly for data analysis in which major, minor, and trace elemental concentrations are used, some form of scaling is necessary to keep the variables with larger concentrations from having excessive weight in the calculation of many coefficients of similarity. [Pg.67]

DDD is a transformation system that operates on expressions of these forms. It as a first-order reasoning tool in which implementation proofs are presented as algebraic derivations. It is proficient at the large-scale formal manipulations involved as structure is imposed on a behavioral specification and as concrete data representations are introduced. A proof consists of an initial expression and a sequence of constructions and transformations together with any side conditions they generate. In practice, one also needs the intermediate expressions in order to address the subexpressions to be manipulated. [Pg.258]

ProcGen generates a scaled 3D model of the test specimen geometry, in the form of a faceted boundary representation. This model is made available for use by other software tasks in the system. The STEP file format (the ISO standard for product data exchange) was chosen to provide future compatibility with CAD models produced externally. In particular part 204 (faceted b-rep) of this standard is used. [Pg.767]

In describing the various mechanical properties of polymers in the last chapter, we took the attitude that we could make measurements on any time scale we chose, however long or short, and that such measurements were made in isothermal experiments. Most of the experimental results presented in Chap. 3 are representations of this sort. In that chapter we remarked several times that these figures were actually the result of reductions of data collected at different temperatures. Now let us discuss this technique our perspective, however, will be from the opposite direction taking an isothermal plot apart. [Pg.256]

Validation and Application. VaUdated CFD examples are emerging (30) as are examples of limitations and misappHcations (31). ReaUsm depends on the adequacy of the physical and chemical representations, the scale of resolution for the appHcation, numerical accuracy of the solution algorithms, and skills appHed in execution. Data are available on performance characteristics of industrial furnaces and gas turbines systems operating with turbulent diffusion flames have been studied for simple two-dimensional geometries and selected conditions (32). Turbulent diffusion flames are produced when fuel and air are injected separately into the reactor. Second-order and infinitely fast reactions coupled with mixing have been analyzed with the k—Z model to describe the macromixing process. [Pg.513]

Two appendices are included at the end of this chapter. The first is intended to serve as a reminder, for those of you who might need it, of the nomendature and representation of stereoisomers. The second appendix contains descriptions of various chemo-enzymatic methods of amino acid production. This appendix has been constructed largely from the recent primary literature and includes many new advances in the field. It is not necessary for you to consult the appendix to satisfy the learning objectives of the chapter, rather the information is provided to illustrate the extensive range of methodology assodated with chemo-enzymatic approaches to amino add production. It is therefore available for those of you who may wish to extend your knowledge in this area. Where available, data derived from die literature are used to illustrate methods and to discuss economic aspects of large-scale production. [Pg.233]

The wavelet interval-tree of scale is constructed fi om log 2 N distinct representations, where N is the number of points in the record of measured data. This is a far more efficient representation than that of scale-space filtering with continuous variation of Gaussian a. [Pg.242]

Bakshi, B. R., and Stephanopoulos, G., Representation of process trends. Part III. Multi-scale extraction of trends from process data. Comput. Chem. Eng. 18, 267 (1994a). [Pg.268]

Fig. 31.1. (a) Score plot in which the distances between representations of rows (wind directions) are reproduced. The factor scaling coefficient a equals 1. Data are listed in Table 31.1. (b) Loading plot in which the distances between representations of columns (trace elements) are preserved. The factor scaling coefficient P equals 1. Data are defined in Table 31.1. [Pg.98]

The computed intensities of the predominant 4f — 4f65d1 transitions, represented by the height of the lines, are well matching the resolution details of the complex experimental spectrum.22 Note that unless there is a global scaling, because of the arbitrary units in experimental data, no fit is implied in the representation of computed results. [Pg.5]

System Representation Errors. System representation errors refer to differences in the processes and the time and space scales represented in the model, versus those that determine the response of the natural system. In essence, these errors are the major ones of concern when one asks "How good is the model ". Whenever comparing model output with observed data in an attempt to evaluate model capabilities, the analyst must have an understanding of the major natural processes, and human impacts, that influence the observed data. Differences between model output and observed data can then be analyzed in light of the limitations of the model algorithm used to represent a particularly critical process, and to insure that all such critical processes are modeled to some appropriate level of detail. For example, a... [Pg.159]

Fig. 25. Rouse-scaling representation of the PEP homopolymer data at 492 K. Above solid lines represents the Ronca model [50] below solid lines display the predictions of local reptation [53]. The solid lines from below tooabove correspond to Q = 0.135 A-1 Q = 0.116 A-1 Q = 0.097 A-1 Q = 0.078 A- Q = 0.068 A-1 Q = 0.058 A-1). The symbols along the lines are data points corresponding to the respective Q-value. (Reprinted with permission from [39]. Copyright 1992 American Chemical Society, Washington)... Fig. 25. Rouse-scaling representation of the PEP homopolymer data at 492 K. Above solid lines represents the Ronca model [50] below solid lines display the predictions of local reptation [53]. The solid lines from below tooabove correspond to Q = 0.135 A-1 Q = 0.116 A-1 Q = 0.097 A-1 Q = 0.078 A- Q = 0.068 A-1 Q = 0.058 A-1). The symbols along the lines are data points corresponding to the respective Q-value. (Reprinted with permission from [39]. Copyright 1992 American Chemical Society, Washington)...
As a signature of the star architecture the elastic scattering data of the completely labelled stars exhibit a pronounced peak at z = 1.5 in the scaled Kratky representation. In contrast to the PI systems, presented before, the Kratky plot of the measured scattering curve disagrees strongly with the prediction of Eq. (123). The experimental halfwidth of the peak is nearly only 50% of the theoretically predicted one. [Pg.101]


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See also in sourсe #XX -- [ Pg.63 ]




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