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Particle plate

Consider here the asymptotic behavior of the potential distribution around a particle (plate, sphere, or cylinder) at large distances, which will also be used for calculating the electrostatic interaction between two particles. [Pg.37]

An alternative approach to this problem is to regard the double layer as a parallel plate condenser in which one plate is the particle surface and the other plate is a plane of counterions at a potential located a distance from the surface and moving with a velocity u relative to the particle surface. If the surface charge density is cr, the electrical force per unit area of the particle plate in a field of unit potential gradient will be a and this force will be balanced by the viscous resistance, which for an assumed Newtonian flow, leads to the equation ... [Pg.60]

The slope of the curves in Fig. 4.36 is only moderately influenced by the reaction order and/or the geometry of the S-phase particles (plates, spheres, or cylinders). However, the form of the curve is strongly affected by the material transport coefficients and/or by in the S phase. Exceptions are possible where rj > 1 due to nonisothermal behavior or complex kinetic equations (Aris, 1975). [Pg.176]

Instead of blending polymers to overcome some of the weaknesses of PLA, particles, plates, and fiber fillers can be used. It would seem that solubility parameters are irrelevant here for composite blends. But it turns out to be very useful to measure the HSP of fillers in order to find one that is optimized for its compatibility with the PLA. If one were designing a new filled system, a good place to start would be one with HSP of (18.6,9.9.6.0) because it would be highly likely to blend in easily and form a stable interface. [Pg.89]

Particles charged in field migrate to earthed plates... [Pg.304]

Impingement demister systems are designed to intercept liquid particles before the gas outlet. They are usually constructed from wire mesh or metal plates and liquid droplets impinge on the internal surfaces of the mist mats or plate labyrinth as the gas weaves through the system. The intercepted droplets coalesce and move downward under gravity into the liquid phase. The plate type devices or vane packs are used where the inlet stream is dirty as they are much less vulnerable to clogging than the mist mat. [Pg.245]

Another type of gravity separator used for small amounts of oily water, the oil interceptor, is widely used both offshore and onshore. These devices work by encouraging oil particles to coalesce on the surface of plates. Once bigger oil droplets are formed they tend to float to the surface of the water faster and can be skimmed off. A corrugated plate interceptor (CPI) is shown below and demonstrates the principle involved. However there are many varieties available. Plate interceptors can typically reduce oil content to 50-150 ppm. [Pg.248]

The flexible large area screen with photostimulable phosphor called the imaging plate, which temporarily stores the image induced by the ionizing radiation, e g. by X-rays, electrons or other charged particles ... [Pg.505]

In the case of a charged particle, the total charge is not known, but if the diffuse double layer up to the plane of shear may be regarded as the equivalent of a parallel-plate condenser, one may write... [Pg.184]

Altliough tire majority of studies on model colloids involve (quasi-) spherical particles, tliere is a growing interest in the properties of non-spherical colloids. These tend to be eitlier rod-like or plate-like. [Pg.2670]

The solid in the tower may be supported on a Witt filter plate, but a plug of glass wool is satisfactory the plug of glass wool above the solid acts as a filter for fine particles of the desiccant. [Pg.184]

Elution volume, exclusion chromatography Flow rate, column Gas/liquid volume ratio Inner column volume Interstitial (outer) volume Kovats retention indices Matrix volume Net retention volume Obstruction factor Packing uniformity factor Particle diameter Partition coefficient Partition ratio Peak asymmetry factor Peak resolution Plate height Plate number Porosity, column Pressure, column inlet Presure, column outlet Pressure drop... [Pg.83]

In these expressions, dp is the particle diameter of the stationary phase that constitutes one plate height. D is the diffusion coefficient of the solute in the mobile phase. [Pg.1108]

Fig. 1.9 Pores in an aggregate composed of plate-like particles. Fig. 1.9 Pores in an aggregate composed of plate-like particles.
We will now consider the dependence of specific surface on particle size for systems composed of particles of simple shape, and exhibiting a distribution of particle sizes. The shapes chosen will, in the first instance, be cubes and spheres, rods, and plates, and will be dealt with in turn. [Pg.30]

Fig. 1.16 Diagrammatic representation of particles, (a) Square plates, of edge length J and thickness t. (h) Square rods, of overall length /, with sides of square having length d. Fig. 1.16 Diagrammatic representation of particles, (a) Square plates, of edge length J and thickness t. (h) Square rods, of overall length /, with sides of square having length d.
From the arguments of the present section it is clear that an inverse relationship holds between the specific surface and the particle size, and if the particles are long or thin it is the minimum dimension, the thickness of the plates or of the rods, which mainly determines the magnitude of the specific surface. [Pg.35]

In the even rarer event that the component particles are equal-sized rods of known length and thickness, or equal-sized platelets of known diameter and thickness, one may respectively use Equation (1.71) with / = 4, or Equation (1.78) with yj, = 2, if the rods or plates are very thin. [Pg.35]

Both (i) and (ii) necessitate recourse to a model of pore shape. By far the commonest, chosen on grounds of simplicity, is the cylinder but the slit model is being increasingly used where the primary particles are plate-like, and the model where the pore is the cavity between touching spheres is beginning to receive attention. [Pg.134]

The pores in question can represent only a small fraction of the pore system since the amount of enhanced adsorption is invariably small. Plausible models are solids composed of packed spheres, or of plate-like particles. In the former model, pendulate rings of liquid remain around points of contact of the spheres after evaporation of the majority of the condensate if the spheres are small enough this liquid will lie wholly within the range of the surface forces of the solid. In wedge-shaped pores, which are associated with plate-like particles, the residual liquid held in the apex of the wedge will also be under the influence of surface forces. [Pg.164]


See other pages where Particle plate is mentioned: [Pg.176]    [Pg.355]    [Pg.172]    [Pg.204]    [Pg.1070]    [Pg.434]    [Pg.23]    [Pg.513]    [Pg.998]    [Pg.97]    [Pg.60]    [Pg.109]    [Pg.176]    [Pg.355]    [Pg.172]    [Pg.204]    [Pg.1070]    [Pg.434]    [Pg.23]    [Pg.513]    [Pg.998]    [Pg.97]    [Pg.60]    [Pg.109]    [Pg.73]    [Pg.304]    [Pg.312]    [Pg.339]    [Pg.505]    [Pg.1047]    [Pg.182]    [Pg.357]    [Pg.1710]    [Pg.1800]    [Pg.1806]    [Pg.428]    [Pg.424]    [Pg.131]    [Pg.321]    [Pg.883]    [Pg.21]    [Pg.23]    [Pg.36]   
See also in sourсe #XX -- [ Pg.633 ]




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