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Yield value, measurement

Influence of Addition of Electrolyte and Increase of Temperature Addition of electrolyte or increase of temperature at a given electrolyte concentration to a sterically stabilized dispersion may result in its flocculation at a critical concentration or temperature, which in many cases coincides with the theta point for the stabilizing chain. At the theta point the mixing term in the steric interaction is zero and any yield value measured should correspond to the residual van der Waals attraction. The energy arising from van der Waals attraction may be calculated from the following approximate relationship,... [Pg.421]

Quantum yield values measured in solution may not necessarily apply to polymer films, the usual environment for practical application of this photochemistry. McKean et al. have adapted the indicator dye method to the measurement of quantum yields for Bronsted acid photogeneration in poly-(4-tert-butoxycarbonyloxystyrene) [20], As with the solution photochemistry of diphenyliodonium salts [71], an inverse dependence of quantum yield on exposure intensity was observed absolute quantum yields from 0.26 to 0.40 were measured at 254 nm, which extrapolate to approximately 0.45 at zero intensity, comparable to the value estimated by Dektar and Hacker [82b] in solution. McKean et al. [20b] note that similar quantum yields in solution and polymer films below Tg have also been reported for photo-Fries rearrangements [84] and photodissociation of diacyl peroxides [85]. [Pg.330]

As mentioned above at the CFC or CFT, AGm= 0 and any yield value measured should correspond to the residual van der Waals attraction. However, as we will see below, the contribution from the van der Waals attraction is small and, therefore, the yield value at the CFC or CFT is very small and unmeasurable. However, as we will also see, above the CFC or CFT, AGm becomes negative and increases significantly with increasing electrolyte concentration and/or temperature leading to measurable revalues. [Pg.105]

The effective surface viscosity is best found by experiment with the system in question, followed by back calculation through Eq. (22-55). From the precursors to Eq. (22-55), such experiments have yielded values of [L, on the order of (dyn-s)/cm for common surfactants in water at room temperature, which agrees with independent measurements [Lemhch, Chem. Eng. ScL, 23, 932 (1968) and Shih and Lem-lich. Am. Inst. Chem. Eng. J., 13, 751 (1967)]. However, the expected high [L, for aqueous solutions of such sldn-forming substances as saponin and albumin was not attained, perhaps because of their non-newtonian surface behavior [Shih and Lemhch, Ind. Eng. Chem. Fun-dam., 10, 254 (1971) andjashnani and Lemlich, y. Colloid Inteiface ScL, 46, 13(1974)]. [Pg.2021]

The Br is a measure of the extent to which viscous heating is important relative to an impressed temperature difference. This can be of some concern in the scale-up design, v usually increasing, with other properties remaining constant. A comparison of the Br for a pilot scale (0.05-m screw) and an industrial (0.15-m screw) unit yields values of ca. 0.65, and 5.73, respectively, for the Br with A = 0.5 w/m K and rj = 500 Pa.s at 60 rpm. The numbers suggest that viscous dissipation will be important and will be much more pronounced in the case of an industrial unit. [Pg.719]

Interpretation of data obtained under the conditions of uniaxial extension of filled polymers presents a severe methodical problem. Calculation of viscosity of viscoelastic media during extension in general is related to certain problems caused by the necessity to separate the total deformation into elastic and plastic components [1]. The difficulties increase upon a transition to filled polymers which have a yield stress. The problem on the role and value of a yield stress, measured at uniaxial extension, was discussed above. Here we briefly regard the data concerning longitudinal viscosity. [Pg.91]

It is interesting to mention here that Dewar and Storch (1989) drew attention to the fact that ion-molecule reactions often lack a transition state barrier in theoretical calculations related to the gas phase, but are known to proceed with measurable activation energy in solution. Szabo et al. (1992) made separate calculations at the ab initio Hartree-Fock 3/21 G level for the geometry of the nitration of benzene with the protonated methyl nitrate by two mechanisms, not involving solvent molecules. Both calculations yielded values for the energy barriers. [Pg.44]

This procedure may seem rather formidable but it readily will be illustrated by a simple example which forms the basis of much of the studies in this area. Consider an aggregate of units with fibre symmetry (i.e. defined by the orientation of a single axis), the aggregate also possessing fibre symmetry. The spectroscopic measurements will then yield values for (cos2 P>, (cos4 P>, etc. The distribution function will be a function of 0 only, and can be expanded in terms of P2(cos 0), P4(cos 0), etc. [Pg.85]

For comparison, Battles et al. (15) determined the partial heats of sublimation of Pu02(g) and Pu0(g) above PuOi.33 over the temperature range 1937 to 2342 K by means of mass spectrometric measurements with Iridium effusion cells. The absence of Iridium oxides or Iridium species In the vapor phase Indicated that Iridium was nonreducing toward plutonia. The partial heats of sublimation calculated from the slopes of the temperature dependency data yielded values of 127.1 1.2 and 138.8 1.6 kcal/mol for Pu0(g) and Pu02(g) ... [Pg.118]

Figure 3.5. Factorial space. Numbers in circles denote process yields actually measured (initial data set) all other numbers are extrapolated process yields used for planning further experiments (assuming that the repeatability Sy = 0.1 all values are rounded to the nearest integer) the estimated yield of 108% shows that the simple linear model is insufficient. Figure 3.5. Factorial space. Numbers in circles denote process yields actually measured (initial data set) all other numbers are extrapolated process yields used for planning further experiments (assuming that the repeatability Sy = 0.1 all values are rounded to the nearest integer) the estimated yield of 108% shows that the simple linear model is insufficient.
The reason for the low C2 selectivity values at high methane conversion and thus the reason for the low measured Ycg and YC2H4 yield values of earlier... [Pg.387]

Figure 7. Dependence of the fluorescence quamum yield of BMPC on solvent viscosity ( ) in linear alcohols, from methanol to dccanol, at 25°C, (o) in absolute ethanol between 200 and 298 K. The quantum yields were measured on optically thin samples (Am <0.2). The value in ethanol, 5.7x10, was determined relative to quinine sulfate in 0.5 mol 1" HjSO ((j)p=0.55 [62]) and 9,10-diphenylanthracene in cyclohexane (4ip=0.90 [63]). It was then used as a reference for the determinations in the other alcohols. Figure 7. Dependence of the fluorescence quamum yield of BMPC on solvent viscosity ( ) in linear alcohols, from methanol to dccanol, at 25°C, (o) in absolute ethanol between 200 and 298 K. The quantum yields were measured on optically thin samples (Am <0.2). The value in ethanol, 5.7x10, was determined relative to quinine sulfate in 0.5 mol 1" HjSO ((j)p=0.55 [62]) and 9,10-diphenylanthracene in cyclohexane (4ip=0.90 [63]). It was then used as a reference for the determinations in the other alcohols.
Other methods of determining the hardness of a material include a variety of "penetration" tests that yield hardness values measured in scales known as the Brinell, Rockwell (B or C), and scleroscope scales. These scales provide reliable hardness values for most materials, including ceramics, glass, metals and alloys, and wood (see Table 21). Unfortunately, as can be seen in the table, the various tests provide somewhat different hardness values for the same materials. [Pg.113]

Equivalent Circuit Analysis. IS measurements yield values of V and Z the real and imaginary components of the impedance, as a function of f, the AC frequency. The data are usually displayed as Nvauist plots (Z, vs. Z ) or Bode plots (impedance modulus,... [Pg.637]

In (8), the solvent-independent constants kr, kQnr, and Ax can be combined into a common dye-dependent constant C, which leads directly to (5). The radiative decay rate xr can be determined when rotational reorientation is almost completely inhibited, that is, by embedding the molecular rotor molecules in a glass-like polymer and performing time-resolved spectroscopy measurements at 77 K. In one study [33], the radiative decay rate was found to be kr = 2.78 x 108 s-1, which leads to the natural lifetime t0 = 3.6 ns. Two related studies where similar fluorophores were examined yielded values of t0 = 3.3 ns [25] and t0 = 3.6 ns [29]. It is likely that values between 3 and 4 ns for t0 are typical for molecular rotors. [Pg.276]

The quantum yield (Q) represents the ratio between the number of photons absorbed and photons emitted as fluorescence. It is a measure of brightness of the fluorophore and represents the efficiency of the emission process. The determination of absolute quantum yield for a fluorophore is experimentally difficult. Therefore, usually relative quantum yield values are determined. To measure the relative quantum yield of a fluorophore, the sample is compared to a standard fluorophore with an established quantum yield that does not show variations in the excitation wavelength [5, 6]. [Pg.239]

The reflectivity R = 0.5[ r + / p ], can be measured. R is independent of both A and 4 and thus provides a third variable. In order to obtain nf, kf and L, values of these parameters are estimated. R, A and T are then calculated from equations (2.84) to (2.92) and compared to the experimentally observed values. nt, kt and Lare altered and the calculations repeated. Regression analysis eventually yields values of the thickness and refractive index of the film that would give rise to the observed R, 4 and A. [Pg.132]


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See also in sourсe #XX -- [ Pg.461 ]




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Measured value

Yield measures

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