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Emulsification failure

FIGU RE 7.13 Maximum of water solubilization versus the parameters influencing the rigidity of the interface and the attraction between water droplets. In the emulsification-failure case, the inside water is expelled by the oil phase. The liquid/liquid phase separation is driven by attractive interaction between micelles in the final state a micellar-poor phase is in equilibrium with a micellar-rich phase. (Readapted from R. Leung and D. O. Shah, J. Colloid Interface Sci., 120(2) 330-344, 1987.)... [Pg.403]

The phase stability of organic extractant phases and classical reverse microemulsions are thus governed by the same rule. This general conclusion would not have been valid for extractant systems in the case of an emulsification failure mechanism, namely rejection of the internal phase, but this was not observed in liquid/liquid extraction systems when salt is extracted. [Pg.403]

Figure 12.2 Regions of stability of spheres, cylinders, and lamellae in oil predicted by a mean-field film theory using Eq. (12-2). The hatched region has coexisting spheres and cylinders. Above the region of spheres, there is a region of emulsification failure, where the sphere phase coexists with an excess water phase. In the ordinate, 8 is the thickness of the surfactant film, which is roughly the surfactant molecular length, 4>a and arc the volume fractions of surfactant (or amphiphile) and water, and / opt = (1 + 0.5k/k)/Ho. (From Safran 1994, with permission from Addison-Wesley Publishing Company, Copyright 1994.)... Figure 12.2 Regions of stability of spheres, cylinders, and lamellae in oil predicted by a mean-field film theory using Eq. (12-2). The hatched region has coexisting spheres and cylinders. Above the region of spheres, there is a region of emulsification failure, where the sphere phase coexists with an excess water phase. In the ordinate, 8 is the thickness of the surfactant film, which is roughly the surfactant molecular length, 4>a and arc the volume fractions of surfactant (or amphiphile) and water, and / opt = (1 + 0.5k/k)/Ho. (From Safran 1994, with permission from Addison-Wesley Publishing Company, Copyright 1994.)...
At the oil-rich side, the phase behaviour is inverted temperature-wise as can be seen in the T( wA)-section provided in Fig. 1.7(c). Thus, the near-critical phase boundary 2 —1 starts at low temperatures from the lower n-octane-QoEs miscibility gap (below <0°C) and ascends steeply upon the addition of water. With increasing wA, this boundary runs through a maximum and then decreases down to the upper critical endpoint temperature Tu. The emulsification failure boundary 1 —r 2 starts at high temperatures and low values of wA, which means that only small amounts of water can be solubilised in a water-in-oil (w/o) microemulsion at temperatures far above the phase inversion. Increasing amounts of water can be solubilised by decreasing the temperature, i.e. by approaching the phase inversion. At Tu the efb intersects the near-critical phase boundary and the funnel-shaped one-phase region closes. [Pg.11]

From the above considerations, it can be concluded that T(wB)- and T(wA)-sections provide an easy method to determine the location of emulsification failure boundaries which are of particular interest if the optimal formulation for an industrial application has to be found. Furthermore, these sections yield the lower and upper temperature of... [Pg.11]

Figure 1.19 Micrographs of microemulsion droplets of the o/w-type in the system II2O- n-octane-CnEs prepared near the emulsification failure boundary at ya = 0.022, wb = 0.040 and T = 26.1 °C. (a) Freeze-fracture direct imaging (FFDI) picture showing dark spherical oil droplets of a mean diameter = 24 9 nm in front of a grey aqueous background. Note that each oil droplet contains a bright domain of elliptic shape which is interpreted as voids, (b) The freeze-fracture electron microscopy (FFEM) picture supports the FFDI result. Each fracture across droplets which contain bubbles shows a rough fractured surface. (From Ref. [26], reprinted with permission of Elsevier.)... Figure 1.19 Micrographs of microemulsion droplets of the o/w-type in the system II2O- n-octane-CnEs prepared near the emulsification failure boundary at ya = 0.022, wb = 0.040 and T = 26.1 °C. (a) Freeze-fracture direct imaging (FFDI) picture showing dark spherical oil droplets of a mean diameter <d> = 24 9 nm in front of a grey aqueous background. Note that each oil droplet contains a bright domain of elliptic shape which is interpreted as voids, (b) The freeze-fracture electron microscopy (FFEM) picture supports the FFDI result. Each fracture across droplets which contain bubbles shows a rough fractured surface. (From Ref. [26], reprinted with permission of Elsevier.)...
Olsson, U. and Schurtenberger, P. (1993) Structure, interactions, and diffusion in a ternary nonionic microemulsion near emulsification failure. Langmuir, 9, 3389-3394. [Pg.83]

An example of such a simple O/W system was investigated with the nonionic surfactant pentaethylene glycol dodecyl ether (C12E5) together with hydrocarbon and water, i.e., the simplest possibility to form a microemulsion (surfactant, oil, water).This system had been studied in some detail before [47-49], and it is well established that it contains spherical aggregates close to the emulsification failure, i.e., when it is saturated with oil. [Pg.362]

The second chapter, by D. Vollmer (Germany), brings a quantitative comparison of experimental data and theoretical predictions on thermodynamic and kinetic properties of microemulsions based on nonionic surfactants. Phase transitions between a lamellar and a droplet-phase microemulsion are discussed. The work is based on evaluation of the latent heat and the specific heat accompanying the transitions. The author focuses on the kinetics of phase separation when inducing emulsification failure by constant heating. The chapter is a comprehensive, detailed study of all the aspects related to the phase separation phenomenon in microemulsions. [Pg.530]

The scheme outlined here has turned out to make up a convenient approach, first, to treating Winsor I and Winsor II microemulsion systems where an excess phase is present [38], in which case it is sufficient to consider merely the first interfacial term of Eq. (191), and, second, to the corresponding one-phase microemulsions elose to the two-phase region (i.e., on the border to what occasionally is referred to as emulsification failure) [47]. [Pg.598]

Winsor also introduced the convenient and popular classification of Winsor I , Winsor IF and Winsor III phase equilibria which are widely found in the literature. Winsor III means that three fluids are in thermodynamic equilibrium, while the other two denominations represent the symmetric cases of emulsification failure Winsor I refers to the case where the excess phase is mainly oil, while Winsor II is that where mainly water is rejected. If the microstructure is made up of isolated droplets, a general assumption - necessary for Bancroft s rule to hold - is made such that the fluid inside the droplets is of similar composition to that of the excess bulk. However, bicontinuous microstructures have been demonstrated to exist whether in Winsor I, Winsor II or Winsor III regimes (10). [Pg.161]

The minimization of the total free energy with the volume fraction of the dispersed phase gives information on the stability of the microemuisions droplets. For small attractive interactions, the microemulsion will demix with an excess of water because of the curvature effect, with this mechanism being called the emulsification failure . On the other hand, for a sufficiently strong attractive droplet interaction, the droplets are destabilized, thus leading to a phase separation of a microemulsion with a smaller droplet volume fraction. [Pg.169]

Figure 9.20. Variation of the packing parameter P(= V/a) as a function of the weight percentage of solute in the oil , lindane a, phenol. P has been determined from the position of the observed emulsification failure in the phase diagram along a water dilution line... Figure 9.20. Variation of the packing parameter P(= V/a) as a function of the weight percentage of solute in the oil , lindane a, phenol. P has been determined from the position of the observed emulsification failure in the phase diagram along a water dilution line...
Minimizing elastic energy in the frame work of the DOC-cylinder model produces connected structures of typical sizes of the order of 100 A. In the absence of solute, electrical percolation is predicted to occur at a volume fraction 0 of 0.35 (Z = 1.2). The microstructure is predicted to be unstable due to emulsification failure for volume fractions lower than 0.33 and higher than 0.48 because it is impossible to minimize the elastic energy under curvature constraints at that point. [Pg.183]

The influence of the presence of an apolar solute on the emulsification failure has been simulated by Nelson et aL (57). The main effect of the presence of an apolar solute is to increase the degrees of freedom in the shape of the aggregates. For example, adding an apolar... [Pg.184]

Figure 15.6. Self-diffusion measurements of the oil component in a microemulsion containing didodecyldimethylammonium sulfate (DDAS)/dodecane/water (D2O) at different ratios of surfactant to oil. The X-axis represents the total volume of oil plus surfactant, i.e. the volume fraction of aggregates/micelles according to equation (15.7) represents oil diffusion when the system solubilizes a maximum amount of oil (the emulsification failure line), with the continuous line being a fit of equation (15.7) to the data represents the oil diffusion at lower oil-to-surfactant ratios when the system forms prolate structures the corresponding line is simply a guide for the eye (Nyden, unpublished data)... Figure 15.6. Self-diffusion measurements of the oil component in a microemulsion containing didodecyldimethylammonium sulfate (DDAS)/dodecane/water (D2O) at different ratios of surfactant to oil. The X-axis represents the total volume of oil plus surfactant, i.e. the volume fraction of aggregates/micelles according to equation (15.7) represents oil diffusion when the system solubilizes a maximum amount of oil (the emulsification failure line), with the continuous line being a fit of equation (15.7) to the data represents the oil diffusion at lower oil-to-surfactant ratios when the system forms prolate structures the corresponding line is simply a guide for the eye (Nyden, unpublished data)...
The phase equilibria at temperatures above To, ((f)-(i)) are essentially mirror images of the behaviour at lower temperatures, with a critical end-point on the oil-rich side at and an emulsification failure boundary, here corresponding to the maximum water solubility, which moves to higher 0s/0w with increasing temperature. [Pg.340]

The Winsor I and Winsor II equilibria (emulsification failure) results from a finite swelling of droplets, and correspond to saturated solutions in equilibrium with excess solubilizate. In the Winsor III equilibrium, the (middle-phase) microemulsion has a bicontinuous structure. Similar to the Winsor I and II equilibria, the three-phase equilibrium can be considered as a finite swelling of the bicontinuous microstructure. The three-phase triangle forms from critical end-points, on the water-rich and one on the oil-rich side. The onset of three phase equilibria appears to be correlated with a micellar to bicontinuous structural transition in the microemulsion phase. [Pg.351]


See other pages where Emulsification failure is mentioned: [Pg.402]    [Pg.554]    [Pg.11]    [Pg.35]    [Pg.37]    [Pg.49]    [Pg.137]    [Pg.138]    [Pg.250]    [Pg.260]    [Pg.260]    [Pg.227]    [Pg.230]    [Pg.25]    [Pg.26]    [Pg.54]    [Pg.126]    [Pg.171]    [Pg.182]    [Pg.287]    [Pg.290]    [Pg.333]    [Pg.339]    [Pg.344]    [Pg.356]   
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See also in sourсe #XX -- [ Pg.339 , Pg.344 , Pg.351 ]

See also in sourсe #XX -- [ Pg.2 , Pg.339 , Pg.344 , Pg.351 ]




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