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Generalization parameters used

In view of the dualism explained above, it may be useful to recall the mutual relationship between the general parameters used in the two approaches. In Smith s treatments, the a.c. polarographic current, I (cot) = AAjF, is generally formulated by [159]... [Pg.343]

Table II. Generalized Parameters Used in the MBWR Equation... Table II. Generalized Parameters Used in the MBWR Equation...
The correlations that are suggested for LLE are UNIQUAC and NRTL f Sorenson and Arlt. 1979. 1980 Macedo and Rasmussen. 1987 Walas, 1985). To obtain useful fits with experimental data specific parameters for the liquid-liquid system, not general parameters used for VLE, should be used (see Appendix B at back of book). If an extraction system will be used for which equilibrium data are unavailable, simulations can be used to determine if the system is worth investigating experimentally (Walas, 1985) however, the LLE must be measured experimentally before the system can be designed with confidence. [Pg.551]

Racah parameters The parameters used to express quantitatively the inter-electronic repulsion between the various energy levels of an atom. Generally expressed as B and C. The ratios between B in a compound and B in the free ion give a measure of the nephelauxetic effect. ... [Pg.339]

Another troublesome aspect of the reactivity ratios is the fact that they must be determined and reported as a pair. It would clearly simplify things if it were possible to specify one or two general parameters for each monomer which would correctly represent its contribution to all reactivity ratios. Combined with the analogous parameters for its comonomer, the values rj and t2 could then be evaluated. This situation parallels the standard potential of electrochemical cells which we are able to describe as the sum of potential contributions from each of the electrodes that comprise the cell. With x possible electrodes, there are x(x - l)/2 possible electrode combinations. If x = 50, there are 1225 possible cells, but these can be described by only 50 electrode potentials. A dramatic data reduction is accomplished by this device. Precisely the same proliferation of combinations exists for monomer combinations. It would simplify things if a method were available for data reduction such as that used in electrochemistry. [Pg.444]

Molecular Connectivity Indexes and Graph Theory. Perhaps the chief obstacle to developing a general theory for quantification of physical properties is not so much in the understanding of the underlying physical laws, but rather the inabiUty to solve the requisite equations. The plethora of assumptions and simplifications in the statistical mechanics and group contribution sections of this article provide examples of this. Computational procedures are simplified when the number of parameters used to describe the saUent features of a problem is reduced. Because many properties of molecules correlate well with stmctures, parameters have been developed which grossly quantify molecular stmctural characteristics. These parameters, or coimectivity indexes, are usually based on the numbers and orientations of atoms and bonds in the molecule. [Pg.255]

For control purposes it is advisable to estimate startup cost and time beforehand and then try to stay within the estimates. Tne general parameters which can be used to estimate startup cost Csu, which are usually between 2 and 20 percent of the batteiy-limit fixed-capital cost, are as follows ... [Pg.874]

Method of Moments The first step in the analysis of chromatographic systems is often a characterization of the column response to sm l pulse injections of a solute under trace conditions in the Henry s law limit. For such conditions, the statistical moments of the response peak are used to characterize the chromatographic behavior. Such an approach is generally preferable to other descriptions of peak properties which are specific to Gaussian behavior, since the statisfical moments are directly correlated to eqmlibrium and dispersion parameters. Useful references are Schneider and Smith [AJChP J., 14, 762 (1968)], Suzuki and Smith [Chem. Eng. ScL, 26, 221 (1971)], and Carbonell et al. [Chem. Eng. Sci., 9, 115 (1975) 16, 221 (1978)]. [Pg.1532]

In addition to qualitative identification of the elements present, XRF can be used to determine quantitative elemental compositions and layer thicknesses of thin films. In quantitative analysis the observed intensities must be corrected for various factors, including the spectral intensity distribution of the incident X rays, fluorescent yields, matrix enhancements and absorptions, etc. Two general methods used for making these corrections are the empirical parameters method and the fimdamen-tal parameters methods. [Pg.342]

Calibration. In general, standards used for instrument calibration are physical devices (standard lamps, flow meters, etc.) or pure chemical compounds in solution (solid or liquid), although some combined forms could be used (e.g., Tb + Eu in glass for wavelength calibration). Calibrated lnstr iment parameters include wavelength accuracy, detection-system spectral responsivity (to determine corrected excitation and emission spectra), and stability, among others. Fluorescence data such as corrected excitation and emission spectra, quantum yields, decay times, and polarization that are to be compared among laboratories are dependent on these calibrations. The Instrument and fluorescence parameters and various standards, reviewed recently (1,2,11), are discussed briefly below. [Pg.100]

As discussed in Chapter 3, the Carreau viscosity model is one of the most general and useful and reduces to many of the common two-parameter models (power law, Ellis, Sisko, Bingham, etc.) as special cases. This model can be written as... [Pg.358]

Charts, correlations, and tables in the sources cited earlier relate capital costs to various parameters characteristic of the equipment to be evaluated. Table B.2 lists typical parameters used to correlate equipment costs for common types of process equipment. Figure B.3 is an example of such correlations for the cost of heat exchangers as a function of exchanger area. These forms of cost curves generally appear as nearly straight lines on log-log plots, indicating a power-law relationship between capital cost and capacity, with exponents typically ranging from 0.5 to 0.8. [Pg.607]

The most useful and important application of Fukui function and local softness resides in the interpretation and thereby, prediction of reaction mechanism, especially in the site selectivity or regioselectivity. Since long FMO theory has generally been used to probe the regioselective nature of a reaction, in particular of organic compounds, but the DFT-based local reactivity parameters have emerged as... [Pg.168]

In contrast, SKM does not assume knowledge of thespecific functional form of the rate equations. Rather, the system is evaluated in terms of generalized parameters, specified by the elements of the matrices A and 0X. In this sense, the matrices A and 0 x are bona fide parameters of the system The pathway is described in terms ofan average metabolite concentration S°, and a steady-state flux vector v°, together defining the metabolic state of the pathway. Additionally, we assume that the substrate only affects reaction v2, the saturation matrix is thus fully specified by a single parameter Of 6 [0,1], Note that the number of parameters is identical to the number used within the explicit equation. The structure of the parameter matrices is... [Pg.196]

In terms of the generalized parameter matrices, the Jacobian is given as product of a simple matrix multiplication. Using explicit kinetic parameters, the estimation of the Jacobian can be tedious and computationally demanding, prohibiting the analysis of large ensembles of models. [Pg.197]

The generalized parameters are invariant with respect to different functional forms of the rate equation. All results hold for a large class of biochemical rate functions [84], For example, the Michaelis Menten rate function used in Eq. (133) is not the only possible choice. A number of alternative rate equations are summarized in Table VI. Although in each case the specific kinetic parameters may differ, each rate equation is able to generate a specified partial derivative and is thereby consistent with results obtained from an analysis of the corresponding Jacobian. Note that, obviously, not each rate equation is capable to generate each possible Jacobian. However, vice versa, for each possible Jacobian there exists a class of rate equations that is consistent with the Jacobian. [Pg.197]

In order to predict pollutant chemodynamics of COMs and/or their leachates, the transport parameters involved in the governing sets of equations that describe the transport process need to be defined accurately [1]. In general, methods used to calculate the transport parameters fall into two broad categories, i. e., steady and transient states. [Pg.200]


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