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Contrast transfer function model

In addition, there are various technical corrections that must be made to the image data to allow an unbiased model of the structure to be obtained. These include correction for the phase-contrast transfer function (CTF) and, at high resolution, for the effects of beam tilt. For crystals, it is also possible to combine electron diffraction amplitudes with image phases to produce a more accurate structure (7), and in general to correct for loss of high resolution contrast for any reason by "sharpening" the data by application of a negative temperature factor (22). [Pg.616]

Models are constructed which suggest that these optical measurements can be used to determine the effective particle size distribution parameters, mean diameter and sigma. Assumptions include multilayer particle deposit, the lognormal distribution of the diameters of the spherical, opaque particles, and no sorting of size classes during particle deposition. The optical measurement include edge trace analysis to derive the contrast transfer function, and density fluctuation measurements to derive the Wiener spectrum. Algorithms to perform these derivations are outlined. [Pg.265]

The correlation analyses of toner particle size and size distribution parameters and image quality characteristics of toner deposits as measured by the spectral dependence of contrast transfer function and noise show high coefficients of correlation Specifically the Wiener spectrum data appear to yield the weight geometric mean and standard deviation of the toner population in this study. Therefore the Wiener spectrum may be another analytical tool in characterizing particle populations. It must be pointed out that the analysis reported here is mainly empirical. Further work is needed to refine the models and to examine the limits of applicability of these tests. Factors such as particle clumping, non-uniform depositions and optical limitations are specific areas for examination. [Pg.277]

Physical Models versus Empirical Models In developing a dynamic process model, there are two distinct approaches that can be taken. The first involves models based on first principles, called physical or first principles models, and the second involves empirical models. The conservation laws of mass, energy, and momentum form the basis for developing physical models. The resulting models typically involve sets of differential and algebraic equations that must be solved simultaneously. Empirical models, by contrast, involve postulating the form of a dynamic model, usually as a transfer function, which is discussed below. This transfer function contains a number of parameters that need to be estimated from data. For the development of both physical and empirical models, the most expensive step normally involves verification of their accuracy in predicting plant behavior. [Pg.6]

We start the LSF analysis by constructing two new transfer functions for the lossless tube. We do this by adding a new additional tube at the glottis, which reflects the backwards travelling wave (whose escape would otherwise cause the loss) into the tube again. As explained in Section 11.3.3, this can be achieved by either having a completely closed or completely open termination. In the closed case, the impedance is infinite, which can be modelled by a reflection coeflBcient value 1, by contrast the open case can be modelled by a coefficient value -1. [Pg.377]

An extension of the notion of relaxation is used when the system is not isolated and continuously perturbed by imposition of an external source of energy. In that case one speaks of forced-relaxation in contrast to the free relaxation described above. The model is the same but instead of establishing the dependence upon time of the state variables during their evolution toward equilibrium, the preferred modeling consists of finding transfer functions, that is, impedance or admittance, featuring the behavior of the system independently from the shape of the perturbation signal. [Pg.513]

Figure 17.8 shows the effect of pole location on the possible responses for a simple first-order transfer function, G(z) = bo/(l - az )y forced by an impulse at A = 0. The corresponding continuous-time model responses are also shown. Poles 3 and 4 are inside the unit circle and thus are stable, while poles 1 and 6 are outside the unit circle and cause an unstable response. Poles 2 and 5 lie on the unit circle and are marginally stable. Negative poles such as 4-6 produce oscillatory responses, even for a first-order discrete-time system, in contrast to continuous-time first-order systems. [Pg.326]

In contrast with the role of cofactor B12 in methionine synthase (methyl group transfer to a thiol), functional Bi2 model complexes have provided a formidable challenge. Several oxime alkyl-cobalt (structural) B12 models when reacted with arene- and alkanethiolates lead only to... [Pg.105]

The first example of a catalytic asymmetric Horner-Wadsworth-Emmons reaction was recently reported by Arai et al. [78]. It is based on the use of a chiral quaternary ammonium salt as a phase-transfer catalyst, 78, derived from cinchonine. Catalytic amounts (20 mol%) of organocatalyst 78 were initially used in the Homer-Wadsworth-Emmons reaction of ketone 75a with a variety of phospho-nates as a model reaction. The condensation products of type 77 were obtained in widely varying yields (from 15 to 89%) and the enantioselectivity of the product was low to moderate (< 43%). Although yields were usually low for methyl and ethyl phosphonates the best enantioselectivity was observed for these substrates (43 and 38% ee, respectively). In contrast higher yields were obtained with phosphonates with sterically more demanding ester groups, e.g. tert-butyl, but ee values were much lower. An overview of this reaction and the effect of the ester functionality is given in Scheme 13.40. [Pg.384]


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Contrast transfer function

Functional modeling

Functional models

Model function

Transfer function

Transfer function functions

Transfer model

Transference function

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