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Particle size properties

The nature of the parent material is the most important factor influencing the mineral components of a soil. In particular, the textural (particle size) properties and inherent fertility are directly affected by the types of rocks and minerals found in the parent material. [Pg.238]

Details of the particle property model may be found in Kiparissides et al M,2] and Chiang and Thompson [3]. Following an approach used by Dickinson [4J and Gorber [5], the development was based on an age distribution analysis in which the classes of particles born between any time, t and T+dt, were followed through the reactor. The result was a series of differential equations in the total particle size properties (diameter, area and volume), the number of particles, conversion and the initiator and emulsifier levels in the reactor. [Pg.210]

A good description of the particle size properties of an aerosolized drug may give some predictive information on its gross behavior within the tracheobronchial tree. Pulmonary deposition studies will, however, always be necessary to bridge between in vitro measurements and the clinical effect. Therefore, determinations of therapeutic equivalence of different formulations should not rely on in vitro measurements alone. Pharmacokinetic measurements of the systemic absorption are used to evaluate whether two formulations are equivalent. In addition, therapeutic equivalence, pharmacodynamic investigations, and, in some instances, in vivo radiolabel deposition studies should be taken into account (8-10). [Pg.146]

Uses Corrosion inhibitor tor clear and pigmented coatings, aq. and soiv.-based coatings, high-solids coatings Features Contains no barium, chromium, or lead low ref. index low oil absorp. very small mean particle size Properties Off-wh. powd. [Pg.136]

Features Lightweight rec. for applies, requiring a finer particle size Properties Gray free-flowing spherical powd. 90-100 mean diam. dens. 0.7-0.8 g/cc bulk dens. 25 Ib/ff soften, pt. 1200 C hardness (Mohs) 5 Toxicology May contain < 5 /o cryst. silica dust may create a respiratory hazard... [Pg.349]

Features Good brightness, controlled particle size Properties Powd. 20 p median particle size 11% on 325 mesh sp.gr. 2.7 dens. 109.5 Ib/ft (tapped) bulk dens. 51 Ib/fl bulking value 22.5 oil absorp. 11 g/100 g brightness 93 Marblewhite 325 [Specialty Mins.]... [Pg.507]

CAS 1332-58-7 EINECS/ELINCS 296-473-8 Uses Filler for adhesives, paints, plastics, and inks Features Delaminated functional filler high brightness, finer particle size Properties Spray-dried beads, slurry 0.6 pm particle diam. 0.01% max. on 325 mesh fineness (Hegman) 5-t- sp.gr. 2.60 bulking value 21.7 lb/ gal surf, area 13-17 mVg oil absorp. 40-45 brightness 90-91 pH 6.0-7.5 (100 gclay/250 ml water)... [Pg.653]

In order to elucidate the derivation of the coalescence birth term in further details, we follow the analysis performed by Sporleder et al. [125]. The analysis can be simplified by considering a problem with only one internal coordinate representing the particle size property. It follows that, if the internal size coordinate is mass or volume, the three particles are related as the size of the child particle equals the sum of the parent particle sizes ... [Pg.975]

When used to separate solid-solid mixtures, the material is ground to a particle size small enough to liberate particles of the chemical species to be recovered. The mixture of solid particles is then dispersed in the flotation medium, which is usually water. Gas bubbles become attached to the solid particles, thereby allowing them to float to the surface of the liquid. The solid partices are collected from the surface by an overflow weir or mechanical scraper. The separation of the solid particles depends on the different species having different surface properties such that one species is preferentially attached to the bubbles. A number of chemicals are added to the flotation medium to meet the various requirements of the flotation process ... [Pg.70]

Rowell and co-workers [62-64] have developed an electrophoretic fingerprint to uniquely characterize the properties of charged colloidal particles. They present contour diagrams of the electrophoretic mobility as a function of the suspension pH and specific conductance, pX. These fingerprints illustrate anomalies and specific characteristics of the charged colloidal surface. A more sophisticated electroacoustic measurement provides the particle size distribution and potential in a polydisperse suspension. Not limited to dilute suspensions, in this experiment, one characterizes the sonic waves generated by the motion of particles in an alternating electric field. O Brien and co-workers have an excellent review of this technique [65]. [Pg.185]

Surface heterogeneity may merely be a reflection of different types of chemisorption and chemisorption sites, as in the examples of Figs. XVIII-9 and XVIII-10. The presence of various crystal planes, as in powders, leads to heterogeneous adsorption behavior the effect may vary with particle size, as in the case of O2 on Pd [107]. Heterogeneity may be deliberate many catalysts consist of combinations of active surfaces, such as bimetallic alloys. In this last case, the surface properties may be intermediate between those of the pure metals (but one component may be in surface excess as with any solution) or they may be distinctly different. In this last case, one speaks of various effects ensemble, dilution, ligand, and kinetic (see Ref. 108 for details). [Pg.700]

One of the most important uses of specific surface determination is for the estimation of the particles size of finely divided solids the inverse relationship between these two properties has already been dealt with at some length. The adsorption method is particularly relevant to powders having particle sizes below about 1 pm, where methods based on the optical microscope are inapplicable. If, as is usually the case, the powder has a raiige of particle sizes, the specific surface will lead to a mean particle size directly, whereas in any microscopic method, whether optical or electron-optical, a large number of particles, constituting a representative sample, would have to be examined and the mean size then calculated. [Pg.37]

Another important area of analytical chemistry, which receives some attention in this text, is the development of new methods for characterizing physical and chemical properties. Determinations of chemical structure, equilibrium constants, particle size, and surface structure are examples of a characterization analysis. [Pg.9]

Physical Properties. Physical properties of importance include particle size, density, volume fraction of intraparticle and extraparticle voids when packed into adsorbent beds, strength, attrition resistance, and dustiness. These properties can be varied intentionally to tailor adsorbents to specific apphcations (See Adsorption liquid separation Aluminum compounds, aluminum oxide (alumna) Carbon, activated carbon Ion exchange Molecular sieves and Silicon compounds, synthetic inorganic silicates). [Pg.278]

The constants a and y depend on the physical and chemical properties of the system, the scmbbing device, and the particle-size distribution in the entering gas stream. [Pg.408]

The raw ROM (run of mine) ore is reduced in size from boulders of up to 100 cm in diameter to about 0.5 cm using jaw cmshers as weU as cone, gyratory, or roU-type equipment. The cmshed product is further pulverized using rod mills and ball mills, bringing particle sizes to finer than about 65 mesh (230 p.m). These size reduction (qv) procedures are collectively known as comminution processes. Their primary objective is to generate mineral grains that are discrete and Hberated from one another (11). Liberation is essential for the exploitation of individual mineral properties in the separation process. At the same time, particles at such fine sizes can be more readily buoyed to the top of the flotation ceU by air bubbles that adhere to them. [Pg.41]

Fluidized-bed design procedures requite an understanding of particle properties. The most important properties for fluidization are particle size distribution, particle density, and sphericity. [Pg.70]


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See also in sourсe #XX -- [ Pg.38 , Pg.42 ]




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