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Independence of components

The half-wave potential is independent of component concentrations. But because of the change in equilibrium potential, the value of polarization in this point depends on the component concentrations. The half-wave potential is usually close to since and differ little in most cases. [Pg.91]

This is the Wigner-Eckart theorem, a very important result which underpins most applications of angular momentum theory to quantum mechanics. It states that the required matrix element can be written as the product of a 3- j symbol and a phase factor, which expresses all the angular dependence, and the reduced matrix element (rj, j T/ (d) if. j ) which is independent of component quantum numbers and hence of orientation. Thus one quantity is sufficient to determine all (2j + 1) x (2k + 1) x (2/ + 1) possible matrix elements (rj, j, mfIkq(A) rj, jf m ). The phase factor arises because the bra (rj, j, m transforms in the same way as the ket (— y m rj, j, —m). The definition of the reduced matrix element in equation (5.123), which is due to Edmonds [1] and also favoured by Zare [4], is the one we shall use throughout this book. The alternative definition, promoted by Brink and Satchler [3],... [Pg.163]

Tables I and II are compilations of the total number of components estimated by using Equation 11 for the five data sets described above. Input data were the peak counts from a series of simulated chromatograms at five different n values for the three different component numbers. The results of Table I were obtained by a counting of baseline resolved peaks. Because these counts are nearly independent of component amplitude, these data are a rather direct test of the validity of the model and procedure. The results of Table II are, by contrast, based upon a counting of peak maxima and upon a calculation of an empirical resolution R. Table III contains data for a comparison of baseline peal counts from the simulated chromatograms to those predicted by theory. Tables I and II are compilations of the total number of components estimated by using Equation 11 for the five data sets described above. Input data were the peak counts from a series of simulated chromatograms at five different n values for the three different component numbers. The results of Table I were obtained by a counting of baseline resolved peaks. Because these counts are nearly independent of component amplitude, these data are a rather direct test of the validity of the model and procedure. The results of Table II are, by contrast, based upon a counting of peak maxima and upon a calculation of an empirical resolution R. Table III contains data for a comparison of baseline peal counts from the simulated chromatograms to those predicted by theory.
Although the Murphree model contains an additional assumption (that the liquid leaving plate j is at its bubble-point temperature) over the modified Murphree model, the corresponding values of y 1 predicted by both models on the basis of the same sets coefficients n Li, nGi and points xylf yj+ lf i appear to be in almost perfect agreement for the two examples presented (see Tables 13-2 and 13-3). These examples were taken from Ref. 24. The number of transfer units for each film in these examples was taken to be independent of component identity just as they are for the existing correlations for binary mixtures which are given below. In Example 13-1 (the benzene-toluene system), the vapor and liquid phases closely approximate ideal solutions, but the liquid phase of the ethanol-water system in Example 13-2 is highly nonideal. [Pg.462]

This result will be employed in conjunction with the thermal energy balance for reactive systems. If there is only one chemical reaction, then subscript j is not required and dFi/vi is independent of component i ... [Pg.66]

Interpenetration of sectors - No industry in today s world can truly claim to be completely independent of components, products, rules of application, etc., that have been developed in other sectors. Bolts are used in aviation and for agricultural machinery welding plays a role in mechanical and nuclear engineering, and electronic data processing has penetrated all industries. Environmentally friendly products and processes, and recyclable or biodegradable packaging are pervasive concerns ... [Pg.149]

As can he seen from Table 1, we have not included all possible component dependencies. For instance, we have through these niunhers stated that components 3 and 4 are independent of component 2. It should also he noted that the way the conditional probabUities are specified reflects the sequence of execution. In this test case the components are assumed to execute sequentially according to their munbers. [Pg.1278]

The first important contribution to atomic stoichiometry in this century seems to be provided by Brinkley (1946). He has shown the importance of the rank of the atomic matrix and presented a proof of the phase rule of Gibbs (1876). A systematic outline of stoichiometry was presented by Petho (sometimes Petheo) and Schay (Petheo Schay, 1954 Schay, Petho, 1962). They gave a necessary and sufficient condition for the possibility of calculating an unknown reaction heat from known ones based upon the rank of the stoichiometric matrix. They introduced the notion of independence of components and of elementary reactions, the completeness of a complex chemical reaction (see the Exercises and Problems) and gave a method to generate a complete set of independent elementary reactions with as many zeros in the stoichiometric matrix as possible (see Petho, 1964). [Pg.28]

We can predict the characteristics of component (b) by Eq. (6.2) (1) cation makes the side on which the solvation is stronger more positive (in potential), while anion X makes the side on which the solvation is stronger more negative (see Fig. 6.3, component (b)) (2) this component is not influenced by electrolyte concentrations. The independence of component (b) from electrolyte concentrations can easily be confirmed. However, the relations of the experimental (actual) variations in component (b) against the values calculated by Eq. (6.2) are somewhat complicated. For the junctions between water and organic solvents (H2O/S), near-linear relations are observed, but the slopes are much smaller than unity, i.e., the average is 0.46 0.029 for five S (i.e., AN, DMF, DMSO, and MeOH) (Fig. 6.6). At the junctions between two aprotic solvents, on the other hand, the slopes are much smaller and, although some contributions of anions and tetraalkylammonium ions are observed, the contributions of alkali metal and silver ions are practically equal to zero... [Pg.177]

As shown in Figure 7-1, the 1 of 2 (2-2-2) Brayton system architecture will always be more reliable than either a 2 of 3 (3-3-3) or a 2 of 4 (4-4-4) Brayton configuration. The results are based on system architecture and are independent of component reliabilities. Three and four Brayton systems have a significant increase in the number of certain components, along with an increase in surface area for redundant components, which negatively impact the reliability of the overall system. The three and four Brayton systems require two Brajrton units to be operable to produce rated system power. [Pg.194]

In this case, there is no superscript on y because, by assumption, Y is independent of pressure. The disadvantage of this procedure is that the reference pressure p" is now different for each component, thereby introducing an inconsistency in the iso-baric Gibbs-Duhem equation [Equation (16)]. In many, but not all, cases, this inconsistency is of no practical importance. [Pg.22]

In general, the flow of key components is constant and independent of the sequence, while the flow of nonkey components varies according to the choice of sequence, as illustrated in Fig. 5.8. [Pg.145]

It is important to note that Eq. (34) becomes independent of the Coriolis term because the symmetrical components of P and ytl cancel it identically. [Pg.56]

Paper chromatography in particular frequently enables the components of a mixture to be separated and identified when only 1-2 mg. of the mixture are available, the process being independent of the relative solubilities of the components. [Pg.48]

Let H and L be two characteristic lengths associated with the channel height and the lateral dimensions of the flow domain, respectively. To obtain a uniformly valid approximation for the flow equations, in the limit of small channel thickness, the ratio of characteristic height to lateral dimensions is defined as e = (H/L) 0. Coordinate scale factors h, as well as dynamic variables are represented by a power series in e. It is expected that the scale factor h-, in the direction normal to the layer, is 0(e) while hi and /12, are 0(L). It is also anticipated that the leading terms in the expansion of h, are independent of the coordinate x. Similai ly, the physical velocity components, vi and V2, ai e 0(11), whei e U is a characteristic layer wise velocity, while V3, the component perpendicular to the layer, is 0(eU). Therefore we have... [Pg.178]

Considering that the pressure is independent of x, integration of the and components of the first-order equation of motion from 0 to x" gives... [Pg.180]

The following three scalars remain independent of the choice of coordinate system in which the components of T are defined and hence are caUed the invariants of tensor T ... [Pg.261]

Furthermore, it is the system. Hydrate I/Hydrate II (or Anhydrous Salt), that possesses a definite pressure at a particular temperature this is independent of the relative amounts, but is dependent upon the nature of the two components in equilibrium. It is incorrect, therefore, to speak of the vapour pressure of a salt hydrate. ... [Pg.41]

Flooding and Pseudo-First-Order Conditions For an example, consider a reaction that is independent of product concentrations and has three reagents. If a large excess of [BJ and [CJ are used, and the disappearance of a lesser amount of A is measured, such flooding of the system with all components butM permits the rate law to be integrated with the assumption that all concentrations are constant except A. Consequentiy, simple expressions are derived for the time variation of A. Under flooding conditions and using equation 8, if x happens to be 1, the time-dependent concentration... [Pg.508]

The simulation models of the flow-sheeting system must make frequent requests for properties at specific temperatures, pressures, and compositions. Computer-program calls for such data are usually made in a rigorously defined manner, which is independent of both the point data generation models and the particular components. These point generation routines provide the property values, using selected methods that base their calculations on a set of parameters for each component. [Pg.76]

For opaque materials, the reflectance p is the complement of the absorptance. The directional distribution of the reflected radiation depends on the material, its degree of roughness or grain size, and, if a metal, its state of oxidation. Polished surfaces of homogeneous materials reflect speciilarly. In contrast, the intensity of the radiation reflected from a perfectly diffuse, or Lambert, surface is independent of direction. The directional distribution of reflectance of many oxidized metals, refractoiy materials, and natural products approximates that of a perfectly diffuse reflector. A better model, adequate for many calculational purposes, is achieved by assuming that the total reflectance p is the sum of diffuse and specular components p i and p. ... [Pg.573]


See other pages where Independence of components is mentioned: [Pg.245]    [Pg.245]    [Pg.412]    [Pg.51]    [Pg.1757]    [Pg.2276]    [Pg.152]    [Pg.245]    [Pg.245]    [Pg.412]    [Pg.51]    [Pg.1757]    [Pg.2276]    [Pg.152]    [Pg.16]    [Pg.44]    [Pg.215]    [Pg.444]    [Pg.411]    [Pg.354]    [Pg.902]    [Pg.2967]    [Pg.119]    [Pg.30]    [Pg.13]    [Pg.231]    [Pg.541]    [Pg.476]    [Pg.512]    [Pg.508]    [Pg.315]    [Pg.397]    [Pg.289]    [Pg.93]    [Pg.248]   
See also in sourсe #XX -- [ Pg.28 ]




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Number of independent components

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