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Equations, regression

Since the a. are themiodynamic quantities, their values fluctuate with time. Thus, (A3.2.141 is properly interpreted as the averaged regression equation for a random process that is actually driven by random... [Pg.696]

This example illustrates how the Onsager theory may be applied at the macroscopic level in a self-consistent maimer. The ingredients are the averaged regression equations and the entropy. Together, these quantities pennit the calculation of the fluctuating force correlation matrix, Q. Diffusion is used here to illustrate the procedure in detail because diffiision is the simplest known case exlribiting continuous variables. [Pg.705]

The regression equation is the best-fit line through the data that minimises the sum of the deviations. [Pg.714]

Vcaic,i is obtained by feeding the appropriate r,- value into the regression equation. Anothe common squared term is the residual sum of squares (RSS), which is the sum of square of the differences between the observed and calculated y values. TSS is equal to the sur of RSS and ESS. The is then given by ... [Pg.715]

The difference between an experimental value and the value predicted by a regression equation. [Pg.118]

Using the Regression Equation Once the regression equation is known, we can use it to determine the concentration of analyte in a sample. When using a normal calibration curve with external standards or an internal standards calibration curve, we measure an average signal for our sample, Yx, and use it to calculate the value of X... [Pg.122]

Substituting the sample s peak current into the regression equation gives the concentration of As(III) as 4.49 X 10 M. [Pg.522]

The optimum modulus occurs at about a 2 1 weight ratio of OTOS to OBTS. Similar optimums have been observed with other accelerator combinations. The examples shown in Figure 4 are calculated from regression equations developed from designed experiments in a black-filled natural mbber compound. On a molar basis, the synergistic accelerator complex appears to consist of two dithiocarbamate ligands and one mercaptobenzothiazole moiety, as shown in stmcture (15) (14). [Pg.227]

Quantitative stmcture—activity relationships have been estabUshed using the Hansch multiparameter approach (14). For rat antigoiter activities (AG), the following (eq. 1) was found, where, as in statistical regression equations, n = number of compounds, r = regression coefficient, and s = standard deviation... [Pg.50]

More recent research provides reversible oxidation-reduction potential data (17). These allow the derivation of better stmcture-activity relationships in both photographic sensitization and other systems where electron-transfer sensitizers are important (see Dyes, sensitizing). Data for an extensive series of cyanine dyes are pubflshed, as obtained by second harmonic a-c voltammetry (17). A recent "quantitative stmcture-activity relationship" (QSAR) (34) shows that Brooker deviations for the heterocycHc nuclei (discussed above) can provide estimates of the oxidation potentials within 0.05 V. An oxidation potential plus a dye s absorption energy provide reduction potential estimates. Different regression equations were used for dyes with one-, three-, five-methine carbons in the chromophore. Also noted in Ref. 34 are previous correlations relating Brooker deviations for many heterocycHc nuclei to the piC (for protonation/decolorization) for carbocyanine dyes the piC is thus inversely related to oxidation potential values. [Pg.396]

The widespread availabihty and utihzation of digital computers for distillation calculations have given impetus to the development of analytical expressions for iregression coefficients that represent the DePriester charts of Fig. 13-14. Regression equations and coefficients for various versions of the GPA convergence-pressure charts are available from the GPA. [Pg.1254]

Figure 4.7 Determination of the linear regression equation manually... Figure 4.7 Determination of the linear regression equation manually...
Basically a regression equation. Suited more to large buoyant plume ai icatioos. [Pg.350]

Regression equation developed from many data... [Pg.350]

With the widespread use of software packages to assist with computational fluid dynamics (CFD) of polymer flow situations, other types of viscosity relationships are also used. For example, the regression equation of Klien takes the form... [Pg.353]

The summations in Eqs. (2-73) are over all i. Equations (2-73) are called the normal regression equations. With the experimental observations of 3, as a function of the Xij, the summations are carried out, and the resulting simultaneous equations are solved for the parameters. This is usually done by matrix algebra. Define these matrices ... [Pg.43]

However, in more recent years it has become usual to employ ar or crR-type constants, either together in the dual substituent-parameter equation or individually in special linear regression equations which hold for particular infrared magnitudes. In this connection a long series of papers by Katritzky, Topsom and their colleagues on Infrared intensities as a quantitative measure of intramolecular interactions is of particular importance. We will sample this series of papers, insofar as they help to elucidate the electronic effects of sulfinyl and sulfonyl groups. [Pg.515]

Some of the species data from Turkana can be compared to those from other areas. Several studies have reported data on non-domestic individuals from various species oiEquus (see Fig. 6.7, data from Bryant e/a/. 1994, 1996 Huertas et al. 1995 Sanchez Chillon et al. 1994 and this study). A recent data compilation (Huertas et al. 1995) resulted in the following regression equation ... [Pg.133]

BI- AND MULTIVARIATE DATA Table 2.1. Linear Regression Equations... [Pg.98]

Gas velocity is an important operating condition in the fluidized bed process and it can highly affect the attrition of dry sorbents. Therefore, the weight remaining in the bed with fluidization time for gas velocity of 20.59 cm/s, 25.74 cm/s, and 30.89 cm/s was measured to estimate the attrition of dry sorbent with gas velocity. As shown in Fig. 4, attrition mainly occurred in the early stage of fluidization. The attrition rate with time decreased and the regression equations fit natural log functions. In addition, Fig. 4 shows that the attrition of dry sorbents is highly affected by gas velocity in the fluidized bed process. [Pg.551]


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