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Partial coefficient plot

The plot of the rate of disappearance of CO per volume of liquid in the serum bottles versus partial pressure of CO in the gas phase based on (3.14.4.14) could give the constant slope value of KLa/H. Henry s constant is independent of the acetate concentration but it is only dependent on temperature. The overall volumetric mass transfer coefficient can be calculated based on the above assumption. The data for various acetate concentrations and different parameters were plotted to calculate the mass transfer coefficient. [Pg.61]

The kinetics of the sulphonation of chlorobenzene have been examined by Kort and Cerfontain176 in order to obtain further information regarding the sulphonation mechanism in very concentrated aqueous sulphuric acid media. First-order rate coefficients (obtained at assorted temperatures) are given in Table 45 and plots of the logarithms of the para partial rate coefficient (used in... [Pg.75]

Here F is the Faraday constant C = concentration of dissolved O2, in air-saturated water C = 2.7 x 10-7 mol cm 3 (C will be appreciably less in relatively concentrated heated solutions) the diffusion coefficient D = 2 x 10-5 cm2/s t is the time (s) r is the radius (cm). Figure 16 shows various plots of zm(02) vs. log t for various values of the microdisk electrode radius r. For large values of r, the transport of O2 to the surface follows a linear type of profile for finite times in the absence of stirring. In the case of small values of r, however, steady-state type diffusion conditions apply at shorter times due to the nonplanar nature of the diffusion process involved. Thus, the partial current density for O2 reduction in electroless deposition will tend to be more governed by kinetic factors at small features, while it will tend to be determined by the diffusion layer thickness in the case of large features. [Pg.267]

To further test the model, calculations were performed to simulate the isotopic tracer experiments presented in Figs. 9 and 10. It should be noted that while the tracer experiments were performed at 438K, the rate coefficients used in the model were chosen to fit the experiments in which chemisorbed NO was reduced at 423 K. Figures 21 and 22 illustrate the nitrogen partial pressure and surface coverage responses predicted for an experiment in which 5 0 is substituted for l NO at the same time that H2 is added to the NO flow. Similar plots are shown in Figs. 23 and 24 for an experiment in which NO is substituted for during steady-state reduction. [Pg.132]

The electrode potentials E Ef) are given in mV and the current densities / in mA/cm. Determine (a) E, the mixed potential (b) / ep, the rate of deposition for this process and (c) the transfer coefficients a for the cathodic and anodic partial reactions. Solve this problem algebraically by finding an intersection of two strait fines do not plot any E = fii) functions. [Pg.167]

Fig. 2. Hill plot for oxygenation of human hemoglobin A as a function of the partial pressure (PO2) of molecular oxygen. The diagram at the right shows that the Hill coefficient will reach a limiting value of one at both extremes of ligand concentration. For this reason this cooperativity index is best measured at ligand concentrations near half-maximal saturation. Fig. 2. Hill plot for oxygenation of human hemoglobin A as a function of the partial pressure (PO2) of molecular oxygen. The diagram at the right shows that the Hill coefficient will reach a limiting value of one at both extremes of ligand concentration. For this reason this cooperativity index is best measured at ligand concentrations near half-maximal saturation.
Sedimentation. The sedimentation experiments are tabulated in Tables I and II. In Table I typical sedimentation coefficients determined in H20 and D20 are in close agreement here and with previously reported values determined for both protio and deuterio phycocyanin from F. calothricoides (15,16). Each of the tabulated coefficients is for a single experiment at an approximate protein concentration of 15 mg. per ml. Lyophilizing a phycocyanin preparation twice had little effect on the observed sedimentation coefficients. In calculating the S values the same partial specific volume of the protein was used for both D20 and H20. This practice is consistent with the recent results of Edelstein and Schach-man (7). Small increases in sedimentation coefficients from H20 to D20 are to be expected because of deuterium substitution on exchangeable positions. The slope of an S vs. concentration plot for phycocyanin in H20 and D20 would also probably differ. Consequently, small changes in S from H20 to D20 would be expected at a constant protein concentration. [Pg.30]

Figure 12. Plot of water image attenuation against a product of factors that reflects the water diffusion rate in a region of interest in ( ) light meat and ( ) dark meat of partially dried sardine. Ag and A0 are the image intensity with and without the gradient pulse for detecting diffusion, respectively. The slope gives the diffusion coefficient, D (cm2/s) D=11.8x lO6 for light meat 8.33 x lO6 for dark meat after eqn.(17) [46]. Figure 12. Plot of water image attenuation against a product of factors that reflects the water diffusion rate in a region of interest in ( ) light meat and ( ) dark meat of partially dried sardine. Ag and A0 are the image intensity with and without the gradient pulse for detecting diffusion, respectively. The slope gives the diffusion coefficient, D (cm2/s) D=11.8x lO6 for light meat 8.33 x lO6 for dark meat after eqn.(17) [46].
When the rejection coefficient equals one, Equation (6.6) reduces to Equation (6.5). A plot of the concentration ratio of retained solute as a function of the volume reduction for membranes with varying rejection coefficients is shown in Figure 6.18. This figure illustrates the effect of partially retentive membranes on loss of solute. [Pg.259]

Partial molar entropies of ions can, for example, be calculated assuming S (H+) = 0. Alternatively, because K+ and Cl ions are isoelectronic and have similar radii, the ionic properties of these ions in solution can be equated, e.g. analysis of B-viscosity coefficients (Gurney, 1953). In other cases, a particular theoretical treatment which relates solvation parameters to ionic radii indicates how the subdivision could be made. For example, the Bom equation requires that AGf (ion) be proportional to the reciprocal of the ionic radius (Friedman and Krishnan, 1973b). However, this approach involves new problems associated with the definition of ionic radius (Stem and Amis, 1959). In another approach to this problem, the properties of a series of salts in solution are plotted in such a way that the value for a common ion is obtained as the intercept. For example, when the partial molar volumes of some alkylammonium iodides, V (R4N+I ) in water (Millero, 1971) are plotted against the relative molecular mass of the cation, M+, the intercept at M + = 0 is equated to Ve (I-) (Conway et al., 1966). This procedure has been used to... [Pg.218]


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See also in sourсe #XX -- [ Pg.237 ]

See also in sourсe #XX -- [ Pg.163 ]




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Partial coefficient

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