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Boundary determination

This profile of the phase boundary determined here looks very similar to that obtained by the mean-field approximation (19), but the result here only applies to the profile above the roughening temperature. Since this is a mean-field theory, fluctuations are also not considered correctly. [Pg.879]

Runaway boundary determined by the existence of ignition (inflection) point in the reaction path analytical equations and graphically presented boundaries in co-ordinates < Se, B> in practice, safe operation if ]/Se> and/or S < 4. [Pg.378]

Data interpretation methods can be categorized in terms of whether the input space is separated into different classes by local or nonlocal boundaries. Nonlocal methods include those based on linear and nonlinear projection, such as PLS and BPN. The class boundary determined by these methods is unbounded in at least one direction. Local methods include probabilistic methods based on the probability distribution of the data and various clustering methods when the distribution is not known a priori. [Pg.45]

Identification of unknown crystal structures and determination of phase fields by X-rays can be problematical if the characteristic patterns of the various phases are quite similar, for example in some b.c.c. A2-based ordered phases in noble-metal-based alloys. However, in many cases the characteristic patterns of the phases can be quite different and, even if the exact structure is not known, phase fields can still be well established. Exact determination of phase boundaries is possible using lattice-parameter determination and this is a well-established method for identifying solvus lines for terminal solid solutions. The technique simply requires that the lattice parameter of the phase is measured as a function of composition across the phase boimdary. The lattice parameter varies across the single-phase field but in the two-phase field becomes constant. Figure 4.12 shows such a phase-boundary determination for the HfC(i i) phase where results at various temperatures were used to define the phase boundary as a fimction of temperature (Rudy 1969). As can be seen, the position of is defined exactly and the method can be used to identify phase fields across the whole composition range. [Pg.99]

Exercise. For the general one-step process (5.1) show that the information n = 0 is an absorbing pure boundary determines the equation for p0 up to one positive constant, as in (7.6b). [Pg.156]

Actually, for r = 6 also the (r, 3)-boundary determines the number of r-gons (see [GHZ02, BDvN06]). [Pg.62]

Fig. 4.16 Phase diagram for aqueous solution of PEO iBio determined using SAXS and rheometry (Pople et al. 1997). The filled symbols mark the phase boundaries determined by SAXS, with the broken line as a guide to the eye, and the solid lines mark transitions determined using rheology (Deng et al. 1995 Pople et al. 1997). The error bars indicate uncertainties associated with the phase transitions determined from repeated heating and cooling ramps. Fig. 4.16 Phase diagram for aqueous solution of PEO iBio determined using SAXS and rheometry (Pople et al. 1997). The filled symbols mark the phase boundaries determined by SAXS, with the broken line as a guide to the eye, and the solid lines mark transitions determined using rheology (Deng et al. 1995 Pople et al. 1997). The error bars indicate uncertainties associated with the phase transitions determined from repeated heating and cooling ramps.
In order to attempt to remove some of these potential ambiguities, more recent developments of this concept have focused on the solubility parameter. The simplest map that can be derived using the solubility parameter is produced with the solubility parameters of the solvents used in solvent separation procedures, and equating these parameters to the various fractions (Figure 3-17). However, the solubility parameter boundaries determined by the values for the eluting solvents that remove the fractions from the adsorbent offer a further step in the evolution of petroleum maps (Figures 3-18 and 3-19). [Pg.130]

In order to predict the ability to propagate an explosion by DSC as described, standard chemicals are needed which fall on the boundary of having ability to propagate explosion or not. The boundary determining chemicals include a mixture of 80% BPO and 20% water and a mixture of 70% 2,4-DNT and 30% inert alumina. [Pg.27]

Above. Range varies with temperature Below. Phase boundaries determined from measurements of unit cell volume... [Pg.28]

The e - y transition boundary was determined by measuring the resistance changes during the transition in a high-compression belt apparatus (Bundy, 1965) and in an internally heated diamond-anvil cell (Boehler, 1986 Mao et al, 1987). The boundary was also determined by in situ X-ray diffraction measurements in an internally heated diamond-anvil cell (Boehler, 1986 Dubrovinsky et al, 1998), in a laser-heated diamond-anvil cell (Shen et al, 1998), and in a multi-anvil apparatus (Funamori et al, 1996 Lfchida et al, 2001). The boundaries determined by Mao et al. (1987), Shen et al (1998), and Lfchida et al (2001) are in good agreement, but are all at —75 K higher temperature (or —2 GPa lower pressure) than the boundary determined by Funamori et al. (1996), Boehler (1986), and Bundy (1965). [Pg.1222]

The separation of xylene isomers on MFl zeolite membranes can be considered one example of intracrystaUine size exclusion and competitive adsorption (strongly dependent on coverage). The difference in their kinetic diameters ( 0.58 nm for p-xylene and 0.68 nm for o- and m-xylene) indicates the possibility of an effective separation using MFl membranes (see Table 10.1). The kinetic diameter of p-xylene is close to one of the MFl channels ( 0.55 nm) whereas o- and m-xylene might be excluded. Therefore, MFl zeolite channels and crystal grain boundaries determinate the permeation characteristics [27]. [Pg.285]

Figure 5. Zirconium hydride phase diagram, showing boundary determination. (After Ref. 11.)... Figure 5. Zirconium hydride phase diagram, showing boundary determination. (After Ref. 11.)...
General Discussion of Faraday s Law. One important point to be observed in connection with Faraday s law is that the amount of electricity passing a boundary determines the total number of chemical equivalents entering into reaction at that point, and not simply the number of equivalents of a single electrochemical reaction. For instance the deposition of zinc from an aqueous solution of one of its salts ... [Pg.27]

The results of moving boundary determinations of transference numbers in which the modern developments of the method have been employed are given in Table IV, and are mainly due to the investigations of Longsworth. The figures in this table will be referred to a number of times in following chapters. The transference numbers are of use in interpreting the results of determinations of the potentials of concentration cells as activity coefficients which, in turn, may be used to test the validity of the thermodynamic aspects of the interionic attraction theory of electrolytes. In addition the transference numbers, alone, and with conductance measurements, are of utility in connection with tests of the interionic attraction theory of electrolytic conductance. [Pg.84]

Table V. Cation Transference Numbers at 25° of Aqueous Solutions of Electrolytes Determined by the Hittorf Method, Compared with the Results of Moving Boundary Determinations... Table V. Cation Transference Numbers at 25° of Aqueous Solutions of Electrolytes Determined by the Hittorf Method, Compared with the Results of Moving Boundary Determinations...
The next question regards the means by which values of any of these quantities to be used in reservoir-engineering calculations may be obtained. There is a continuing history of theoretical attempts to calculate the mobility of foam starting from known quantities and familiar principles of two-phase flow in porous rocks. One of these principally considers the effect of capillary pressure and concludes that this quantity is a principal determinant of the stability and therefore of the population of lamellae. Presuming equilibrium conditions in which the radii of curvature of the Plateau boundaries determines the excess of absolute pressures in the gas over that in the liquid, Khatib et al. (16) computed a limiting value of the capillary pressure. Above this value, the lamellae become too thin for the surfactant to stabilize. Increasing the gas fractional flow decreases the water saturation and raises the capillary pressure. [Pg.217]

The NMR line widths can be used to determine phase transitions in both one- and multicomponent mesomorphic systems. Transition temperatures and phase boundaries determined by NMR are usually in good agreement with those determined by other methods. The NMR data can therefore be used to construct reliable phase diagrams. They are most useful in systems where separation of the mesophase from other phases is difficult or impossible. [Pg.56]

Irrespective of the differences between in situ and ex situ measurements (see below and Chapter 6), there are generally two ways to determine the transport rates of dissolved substances across the water/sediment boundary determination of the concentration differences along the depth profiles (gradient approach) and measurement of the time-dependent concentration changes of dissolved species within a closed... [Pg.431]

PHASE BOUNDARY DETERMINATIONS OF BINARY MIXTURES AT LOW TEMPERATURES ... [Pg.177]

The apparatus employed for the investigation is based on a modified version of the dew and bubble-point method of phase-boundary determination. By altering the standard procedure, solid-liquid-vapor and solid-vapor equilibria data can be determined along with the vapor-liquid data in the same basic apparatus used for dew and bubble-point measurements. The method presented here is a slight variation of the method presented by Kurata and Kohn [ ] and similar to that of Donnelly and Katz p]. [Pg.177]

Phase Boundary Determinations of Binary Mixtures at Low Temperatures... [Pg.183]


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See also in sourсe #XX -- [ Pg.26 ]




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