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Particles emulsion

What happens during hydrolysis is that the OH forms and the elemicin propyl alcohol drops out of solution and forms its own oil layer. Of course one won t see this because the solution is a big old brown mess, lousy with emulsion particles. Emulsions suck But can be dealt with effectively by adding a little acid or base, or filtration and the like. Anyway, after a little work up one gets some really pure phenylpropyl compound. And if Strike had Strike s way. Strike would have that OH stuck right on the middle (beta) carbon of the species. Work could then progress on using that OH to get an amphetamine (Sob Strike had so much about that subject that Strike was prepared to put in this book ). [Pg.51]

Broadly speaking, for G/S systems, three modes of particle-fluid contacting may be recognized to take place simultaneously as shown in Fig. 43 bubbles containing sparsely disseminated particles, emulsion of densely suspended particles, and defluidized (transient as well as persistent) particles not fully suspended hydrodynamically by the flowing gas. For all intents and purposes, it is desirable to suppress bubbles and to prevent defluidization. [Pg.556]

The easiest model to treat theoretically is the sphere, and many colloidal systems do, in fact, contain spherical or nearly spherical particles. Emulsions, latexes, liquid aerosols, etc., contain spherical particles. Certain protein molecules are approximately spherical. The crystallite particles in dispersions such as gold and silver iodide sols are sufficiently symmetrical to behave like spheres. [Pg.6]

As pointed out in Chapter 8, the forces of centrifugation are too weak to influence the distribution of small molecules. The molecular weight M of species must be 106 in order to generate the necessary force in SdFFF. However for M > 106, there are many important separation problems involving polymers, biological macromolecules (such as DNAs), subcellular particles, emulsions, and a great variety of natural and industrial colloids. SdFFF has been applied to many such systems [10-12,16]. An example of the separation of colloidal polystyrene latex microspheres is shown in Figure 9.9,. [Pg.203]

Electrophoresis — Movement of charged particles (e.g., ions, colloidal particles, dispersions of suspended solid particles, emulsions of suspended immiscible liquid droplets) in an electric field. The speed depends on the size of the particle, as well as the -> viscosity, -> dielectric permittivity, and the -> ionic strength of the solution, and it is directly proportional to the applied electric field. In analytical as well as in synthetic chemistry electrophoresis has been employed to separate species based on different speeds attained in an experimental setup. In a typical setup the sample is put onto a mobile phase (dilute electrolyte solution) filled, e.g., into a capillary or soaked into a paper strip. At the ends of the strip connectors to an electrical power supply (providing voltages up to several hundred volts) are placed. Depending on their polarity and mobility the charged particles move to one of the electrodes, according to the attained speed they are sorted and separated. (See also - Tiselius, - electrophoretic effect, - zetapotential). [Pg.236]

Gels are of central importance for most semisolid food products. A gel can contain more than 99% water and still retain the characteristics of a solid. The network structure will determine whether the water will be firmly held or whether the gel will behave more like a sponge, where water is easily squeezed out. The gel structure will also have a major impaet on the texture as well as diffusion of water and soluble compounds. Many food matrixes are based on colloidal gels such as yoghurts, cheeses, many desserts, sausages etc (see also Chapters 19 and 20). In whole foods, there is often a combination of colloidal structures and fragments of biological tissues or gel structures in combination with particles, emulsion and foam structures. This level of complexity of composite food structures will not be dealt with here. [Pg.255]

There are four main types of liquid-phase heterogeneous free-radical polymerization microemulsion polymerization, emulsion polymerization, miniemulsion polymerization and dispersion polymerization, all of which can produce nano- to micron-sized polymeric particles. Emulsion polymerization is sometimes called macroemulsion polymerization. In recent years, these heterophase polymerization reactions have become more and more important... [Pg.3]

Number of particles. Emulsion polymerization of 1,4-DVB yields significantly more and smaller polymer particles than that of styrene (table I). [Pg.94]

The sedimentation FFF is shown schematically in Fig. 2a. The separation channel is situated inside a centrifuge rotor and the centrifugal forces are applied radially [8]. The method can be used for the analysis and characterization of various latexes, inorganic particles, emulsions, biological cells, and so forth. The retention parameter A depends on the effective mass of the particles ... [Pg.678]

In the presence of surfactant along with poly(vinyl alcohol) finer particlesized latices are formed. The emulsions form clear, glossy films. On addition of borax, such latices may be coagulated. Combinations of synthetic colloids with siurfactants may produce fine-particle emulsions stable to borax and other additives such as starches, dextrines, and salt. Many natural gums have been used as protective colloids along with surfactants to produce fine-particle, water-resistant, borax-stable emulsions [128]. [Pg.254]

Atoms and molecules Colloidal particles Emulsions and suspensions... [Pg.28]

So far, we tacitly assumed that the colloidal particles are rigid, so that they do not deform upon approach. This assumption more or less holds for solid particles. However, for fluid particles, as present in emulsions and foams, deformations may easily occur and they invoke additional mechanisms affecting their stability. In this chapter, we restrict ourselves to nondeformable particles. Emulsions and foams are discussed in Chapter 18. [Pg.307]

The stability of these systems is generally achieved through a protective interfacial layer around the particles (emulsion droplets or foam bubbles). The properties of this interfacial layer are governed by the composition and structure of the adsorbed material and in turn would determine the properties of the dispersion [3]. [Pg.138]

The rise velocity of the bubble, relative to the gas/ particle emulsion, is... [Pg.282]

Flotation processes are an important part of water treatment technologies in modern water treatment plants. Flotation is based on the principle of adhesion of insoluble particles to air bubbles and adsorption of dissolved surfactants at the surface of air bubbles. Flotation allows for different kinds of admixtures to be removed from water bulk in a physical and chemical manner. In this way, suspended and colloidal particles, emulsions of oils and fats, the separate surfactant molecules and their micelles, complexes of surfactants with colloid rust, and multivalent ions of heavy metals can be removed. At present, the flotation processes and equipment for their realization are widely described in the literature [12]. Flotation involves the injection of small bubbles of air or other gas into the water bulk. Surface-active impurities are adsorbed at the bubble surface and transferred through the water bulk to its surface. As a result, the foam concentrate is formed on the surface of bubbling water. It contains surfactants, suspended solid particles (water impurities), emulsified substances, bacterial cells, etc. This foam is evacuated from the surface by means of special scrapers and other devices. [Pg.494]

As well as these static—essentially geometric—effects that produce depletion at the wall, there are also dynamic effects which enhance the phenomenon. The existence of a shear rate and/or a shear rate gradient in the fluid next to the wall (as in a pipe) results in a further movement of particles away from the wall, towards areas of lower shear rates such as the centre of pipes. Solid particles, emulsion droplets and polymer molecules all show this tendency. [Pg.134]

The rheology of dispersions of liquid particles (emulsions) has also been largely investigated. If the droplets retain their spherical shape under shear, the continuous medium is Newtonian and the dispersion is diluted enough the emulsion behaves as Newtonian with viscosity given by Taylor equation [30]... [Pg.245]

There are two polymerization processes widely used to produce attaching to functionalized latex particles emulsion homopolymerization of a monomer containing the desired functional group (functionalized monomer) and emulsion copolymerization of styrene (usually) with the functionalized monomer. The following paragraphs present some of the more relevant contributions in this field. [Pg.270]

In the drying stage at the end of water evaporation the particles adopt a hexagonal dose-packed geometry. Good subsequent film formation requires a high level of polymer particle deformability and the rapid interdiffusion of polymer chains between the particles. Emulsion polymers therefore possess a so-called minimum film formation temperature (MET), below which no compact film can be formed. The determination of the MET is discussed below. [Pg.59]


See other pages where Particles emulsion is mentioned: [Pg.199]    [Pg.9]    [Pg.50]    [Pg.199]    [Pg.490]    [Pg.329]    [Pg.105]    [Pg.264]    [Pg.131]    [Pg.66]    [Pg.221]    [Pg.190]    [Pg.1607]    [Pg.137]    [Pg.199]    [Pg.226]    [Pg.89]    [Pg.3379]    [Pg.106]    [Pg.302]    [Pg.443]    [Pg.144]    [Pg.806]    [Pg.262]    [Pg.102]    [Pg.376]   
See also in sourсe #XX -- [ Pg.79 ]




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Dispersed particles, emulsions

Dispersed particles, emulsions forces

Emulsion Polymerizations in Nonuniform Latex Particles

Emulsion measuring particle swelling

Emulsion monomer concentration inside particle

Emulsion particle aggregation

Emulsion particle formation

Emulsion particle size distribution

Emulsion particle-electrolyte interaction

Emulsion particles, light scattering studies

Emulsion polymerization heterogeneous particles

Emulsion polymerization particle encapsulation

Emulsion polymerization particle morphology

Emulsion polymerization particle nucleation

Emulsion polymerization particle number

Emulsion polymerization particle size

Emulsion polymerization particle size distribution

Emulsion polymerization particle stability

Emulsion polymerization particle surface character

Emulsion polymerization particles

Emulsion polymerizations particle size optimization

Emulsion rubbery particles

Emulsion solid particles

Emulsion systems, particle size

Emulsion systems, particle size distributions, study

Emulsions Vegetable particle sizing

Emulsions mean particle size

Emulsions particle size analysis

Encapsulation of Solid Particles by the Concentrated Emulsion Polymerization Method

Inverse emulsion polymerization, particle

Latex emulsion polymerization particle

Latex particles surface functionalization seeded emulsion copolymerization

Light scattering emulsion polymer particles

Particle clustering emulsion phase

Particle concentration, emulsions

Particle concentration, emulsions flocculation

Particle diameter, emulsions, effect

Particle formation rate, emulsion

Particle in emulsion polymerization

Particle nucleation in emulsion polymerization

Particle size distribution emulsions, effect

Particle size distribution in emulsion polymerization

Particle size distribution multiple emulsions

Particle size in emulsions

Particle size, emulsions

Particle size, emulsions concentration

Particle size, emulsions flocculation

Particle stabilized emulsion

Particle swelling of carboxylic emulsion

Particles from Emulsions

Poly emulsion particle formation

Polymer-Clay Nanocomposite Particles by Inverse Emulsion Polymerization

Scattering emulsion polymer particles

Simple Emulsions Stabilized by Solid Particles

Solid Particles at Liquid Interfaces, Including Their Effects on Emulsion and Foam Stability

Styrene emulsion particle size

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