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Critical flocculation volume

Attempts to measure a critical flocculation volume of nonsolvent by titration with non-solvent as used by Napper (4) were not successful. A sharp transition between a relatively stable dispersion and a sudden loss of all colloidal stability was never observed and no unambiguous end-points could be detected. [Pg.300]

The crucial question is at what value of <)> is the attraction high enough to induce phase separation De Hek and Vrij (6) assume that the critical flocculation concentration is equivalent to the phase separation condition defined by the spinodal point. From the pair potential between two hard spheres in a polymer solution they calculate the second virial coefficient B2 for the particles, and derive from the spinodal condition that if B2 = 1/2 (where is the volume fraction of particles in the dispersion) phase separation occurs. For a system in thermodynamic equilibrium, two phases coexist if the chemical potential of the hard spheres is the same in the dispersion and in the floe phase (i.e., the binodal condition). [Pg.252]

The stability of these dispersions has been investigated. A strong dependence of critical flocculation conditions (temperature or volume fraction of added non-solvent) on particle concentration was found. Moreover, there seems to be little or no correlation between the critical flocculation conditions and the corresponding theta-conditions for the stabilising polymer chains, as proposed by Napper. Although a detailed explanation is difficult to give a tentative explanation for this unexpected behaviour is suggested in terms of the weak flocculation theory of Vincent et al. [Pg.281]

The stability of the various dispersions was assessed and compared by determining the critical flocculation conditions (temperature or volume fraction of added non-solvent for the grafted polymer), as a function of particle concentration. [Pg.283]

Figure 3. Critical flocculation temperature (T) versus log (particle volume fraction ) for the two Si02 g PDMS dispersions in bromocyclohexane O, S15/PDMS5 x, S15/ PDHS3. Figure 3. Critical flocculation temperature (T) versus log (particle volume fraction <f>) for the two Si02 g PDMS dispersions in bromocyclohexane O, S15/PDMS5 x, S15/ PDHS3.
Figure 4. Critical flocculation solvent composition toluene + n-hexane (v = volume fraction of toluene), versus log (particle volume fraction, (J>) for various SiC -g-PS systems at 24 1°C V, S12/PS13c 0, S12/PS13a ... Figure 4. Critical flocculation solvent composition toluene + n-hexane (v = volume fraction of toluene), versus log (particle volume fraction, (J>) for various SiC -g-PS systems at 24 1°C V, S12/PS13c 0, S12/PS13a ...
It was suggested in a previous publication (9) that flocculation at the UCFT can be ascribed to the free volume dissimilarity between the polymer stabilizing the particle and the low molecular weight dispersion medium. Incorporating this idea in a quantitative way into the theory of steric stabilization allowed for a qualitative interpretation of the experimental data. This idea is further extended to include the effect of pressure on the critical flocculation conditions. [Pg.323]

When >0.5, becomes negative (attractive) this, combined with the van der Waals attraction at this separation distance, produces a deep minimum causing flocculation. In most cases, there is a correlation between the critical flocculation point and the 0-condition of the medium. A good correlation is found in many cases between the critical flocculation temperature (CFT) and the 0-temperature of the polymer in solution (with both block and graft copolymers the 0-temperature of the stabilising chains A should be considered) [2]. A good correlation was also found between the critical volume fraction (CFV) of a nonsolvent for the polymer chains and their 0-point under these conditions. In some cases, however, such correlation may break down, and this is particularly the case for polymers that adsorb by multipoint attachment. This situation has been described by Napper [2], who referred to it as enhanced steric stabilisation. [Pg.122]

For example, the emulsion will flocculate at a temperature (referred to as the critical flocculation temperature CFT) that is equal to the 0-temperature of the stabilising chain. The emulsion may flocculate at a critical volume fraction (CFV) of a nonsolvent, which is equal to the volume of nonsolvent that brings it to a... [Pg.195]

Flocculated Systems. The viscoelastic responses of flocculated systems are strongly dependent on the suspension structure. The suspension starts to show an elastic response at a critical solid volume fraction of 0ct = 0.05 — 0.07, at which the particles form a continuous three-dimensional network (211-213). The magnitude of the elastic response for flocculated suspensions above 0ct depends on several parameters, such as the suspension structure, interparticle attraction forces and particle size, and shape and volume fraction. Buscall et al. (10) found that the volume fraction dependence of the storage modulus follows a power-law behavior. [Pg.166]

S.4. Critical flocculation particle volume fraction Theoretical considerations... [Pg.170]

It is usually easier experimentally to specify the critical particle volume fraction rather than the critical particle concentration. Vincent, who has pioneered this approach, usually denotes the critical coagulation particle volume fraction by CF4>. The in Vincent s pseudo-acronym denotes the particle volume fraction whereas the F denotes flocculation, rather than the term coagulation which has been preferred in this text to signify the origin of the attraction. [Pg.172]

Depletion flocculation is produced by addition of a free nonadsorbing polymer [7]. In this case, the polymer coils caimot approach the particles to a distance A (this is determined by the radius of gyration of free polymer, Rq), as the reduction in entropy on close approach of the polymer coils is not compensated by an adsorption energy. The suspcakesension particles or emulsion droplets will be surrounded by a depletion zone with thickness A. Above a critical volume fraction of the free polymer, the polymer coils wiU be squeezed out from between the particles... [Pg.122]

This is achieved by the addition of free (nonadsorbing) polymer in the continuous phase [26]. At a critical concentration, or volume fraction of free polymer,, weak flocculation occurs as the free polymer coils become squeezed-out from between the droplets. This is illustrated in Figure 10.27, which shows the situation when the polymer volume fraction exceeds the critical concentration. [Pg.191]


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See also in sourсe #XX -- [ Pg.98 , Pg.104 , Pg.105 , Pg.107 , Pg.108 , Pg.109 , Pg.111 , Pg.118 , Pg.170 , Pg.185 ]




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Critical flocculation volume fraction

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