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Volume fractional additivity

At lower Na+ concentration, the high negative charge (zeta potentials of salt-free emulsion droplets are 115 mv and above (5)) immobilizes a water layer around the droplets, thus effectively increasing the apparent volume fraction. Addition of Na+ reduces the net charge and some of the immobilized water is released giving a lower apparent volume fraction and lower apparent viscosity. [Pg.482]

Another factor which may become increasingly important is the flash point. Unfortunately there is no simple relation to estimate flash points of mixtures, so this limits the accuracy of flash paint restrictions in the linear programming technique. We have included an option to maintain the flash point above a given value. Since the additivity is based on simple volume fraction additivity of the flash points, this option can only be considered a very rough guide. [Pg.61]

Substituting f(e) function into [9.23], we obtain volume-fractional additivity of permittivity... [Pg.513]

For systems formed of two associated liquids, there are no reliable methods of isotherms calculation. An empirical method has been proposed, which is based on the assumption that each associated component mixed with the other associated component that does not interact chemically with the first one introduces the rigorously defined contribution into deviation from the volume-fractional additivity. The extent of these deviations for the first representatives of the series of aliphatic carbonic acids and alcohols of normal structure, as well as for some phenols, are given elsewhere. ... [Pg.514]

The HLB system has made it possible to organize a great deal of rather messy information and to plan fairly efficient systematic approaches to the optimiza-tion of emulsion preparation. If pursued too far, however, the system tends to lose itself in complexities [74]. It is not surprising that HLB numbers are not really additive their effective value depends on what particular oil phase is involved and the emulsion depends on volume fraction. Finally, the host of physical characteristics needed to describe an emulsion cannot be encapsulated by a single HLB number (note Ref. 75). [Pg.514]

Since Api and Ap2 are both obtained from differentiating the same expression for AGj, it makes no difference which of these we work with further. In addition, it makes no difference whether we differentiate with respect to X2 or Xi, since dxi = -dx2 and we are setting the results equal to zero. Furthermore, since higher derivatives will be set equal to zero, we can differentiate with respect to volume fraction instead of mole fraction. This is because 9/9x =... [Pg.532]

Rheology. The rheology of foam is striking it simultaneously shares the hallmark rheological properties of soHds, Hquids, and gases. Like an ordinary soHd, foams have a finite shear modulus and respond elastically to a small shear stress. However, if the appHed stress is increased beyond the yield stress, the foam flows like a viscous Hquid. In addition, because they contain a large volume fraction of gas, foams are quite compressible, like gases. Thus foams defy classification as soHd, Hquid, or vapor, and their mechanical response to external forces can be very complex. [Pg.430]

Although aH these models provide a description of the rheological behavior of very dry foams, they do not adequately describe the behavior of foams that have more fluid in them. The shear modulus of wet foams must ultimately go to zero as the volume fraction of the bubbles decreases. The foam only attains a solid-like behavior when the bubbles are packed at a sufficiently large volume fraction that they begin to deform. In fact, it is the additional energy of the bubbles caused by their deformation that must lead to the development of a shear modulus. However, exactly how this modulus develops, and its dependence on the volume fraction of gas, is not fuHy understood. [Pg.430]

Immiscible Blends. When two polymers are blended, the most common result is a two-phase composite. The most interesting blends have good adhesion between the phases, either naturally or with the help of an additive. The barrier properties of an immiscible blend depend on the permeabihties of the polymers, the volume fraction of each, phase continuity, and the aspect ratio of the discontinuous phase. Phase continuity refers to which phase is continuous in the composite. Continuous for barrier appHcations means that a phase connects the two surfaces of the composite. Typically, only one of the two polymer phases is continuous, with the other polymer phase existing as islands. It is possible to have both polymers be continuous. [Pg.496]

Thus the addition of the stiff carbon fibers has a very great effect in stiffening the epoxy matrix. Eor the commonly used fiber volume fraction of 0.6 the unidirectional carbon—epoxy lamina has a predicted extensional stiffness E = 145 GPa (2.1 x 10 psi)-... [Pg.10]

Under these conditions the reciprocal relationship fits the data extremely well, particularly at volume fractions below 0.5 of the strongly eluting solute. In addition, under these conditions the inverse will also apply, i.e.,... [Pg.112]

In addition it may be seen that the strengthening effect of the fibres is only observed (i.e. a u > volume fraction is greater than a certain... [Pg.176]

The results of the micromechanics studies of composite materials with unidirectional fibers will be presented as plots of an individual mechanical property versus the fiber-volume fraction. A schematic representation of several possible functional relationships between a property and the fiber-volume fraction is shown in Figure 3-4. In addition, both upper and lower bounds on those functional relationships will be obtained. [Pg.125]

In order to draw the property - composition diagram, coordinates are usually chosen so that the ideal system values correspond with the additive law regarding concentration [313]. It is known, for instance, that in an ideal system, molar volume changes additively with the concentration, and is expressed in molar fractions or molar percentages, whereas specific volume changes linearly with the concentration, and is expressed in mass fractions or mass percentages. [Pg.148]

Addition of both ion-conducting and inert ceramics enhances the conductivity of a polymer electrolyte. This increase is attributed to an increase in volume fraction of the amorphous phase [133-136]. No... [Pg.518]

Figure 18.1 is the typical stress-strain curves of the filled rubber (SBR filled with fine carbon black, HAF),

Figure 18.1 is the typical stress-strain curves of the filled rubber (SBR filled with fine carbon black, HAF), <p the volume fraction of carbon black, showing the above three criteria from 1 to 3. The most characteristic point in stress-strain relation of the filled rubber is first, that the stress increase becomes larger and larger as extension increases (called the stress upturn), in addition to the initial stress (modulus) increase at small extension. Second, the tensile strength is 10-15 times larger than that of the unfilled rubber vulcanizate whose strength is in the order of 2 or 3 MPa ( = 0 in Figure 18.1). Moreover, the tensile strain is also quite large, compared with the unfilled rubber of the same modulus, as shown in Figure 18.1.
VOF or level-set models are used for stratified flows where the phases are separated and one objective is to calculate the location of the interface. In these models, the momentum equations are solved for the separated phases and only at the interface are additional models used. Additional variables, such as the volume fraction of each phase, are used to identify the phases. The simplest model uses a weight average of the viscosity and density in the computational cells that are shared between the phases. Very fine resolution is, however, required for systems when surface tension is important, since an accurate estimation of the curvature of the interface is required to calculate the normal force arising from the surface tension. Usually, VOF models simulate the surface position accurately, but the space resolution is not sufficient to simulate mass transfer in liquids. [Pg.341]

Effects of additives (electrolytes, surfactants, nonelectrolytes) on the volume fraction and temperature percolation thresholds of a water/AOT/n-heptane system have been investigated [280,281]. [Pg.496]


See other pages where Volume fractional additivity is mentioned: [Pg.20]    [Pg.124]    [Pg.20]    [Pg.124]    [Pg.242]    [Pg.195]    [Pg.7]    [Pg.419]    [Pg.438]    [Pg.89]    [Pg.201]    [Pg.290]    [Pg.57]    [Pg.186]    [Pg.471]    [Pg.185]    [Pg.149]    [Pg.152]    [Pg.688]    [Pg.1112]    [Pg.438]    [Pg.166]    [Pg.177]    [Pg.300]    [Pg.307]    [Pg.330]    [Pg.572]    [Pg.578]   
See also in sourсe #XX -- [ Pg.413 ]




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