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Particle form

spherical materials are the technical state of the art. Mostly, they can be packed easily and give a good performance. [Pg.247]

The particle size, dp, is the mean particle diameter and is normally indicated in micro meter. The particle size defines two important values  [Pg.247]

If the number of plates is increased by using smaller particles then, as a consequence, the pressure increases by square at the same rate. [Pg.247]

In this context, the particle size distribution is especially important. An increased share of small particles, especially, increases the back pressure. When there are more bigger particles, the number of plates decreases. An additional problem of a broad particle size distribution is that the material is more difficult to pack. [Pg.247]

If pressure-sensitive soft gels are used and the amount of small particles, so-called fines, is too high, this of course directly influences the field of application (flow rate, column length). In the case of analytical separations, this often does not matter much, because pre-packed columns are mostly used. In the case of preparative purifications, however, a column with a low number of plates and an increased back pressure negatively influences the loading, purity, run time, and lifetime. [Pg.247]


In the case of powders formed by grinding and particles formed by aggregation, surface roughness can be so extreme that, curiously, it can be treated by mathematical geometry (see Mandelbrot, Ref. 102 also Ref. 103). We can... [Pg.272]

It will be convenient to deal first with the distribution aspect of the problem. One of the clearest ways in which to represent the distribution of sizes is by means of a histogram. Suppose that the diameters of SOO small spherical particles, forming a random sample of a powder, have been measured and that they range from 2-7 to 5-3 pm. Let the range be divided into thirteen class intervals 2-7 to 2-9 pm, 2-9 to 3-1 pm, etc., and the number of particles within each class noted (Table 1.5). A histogram may then be drawn in which the number of particles with diameters within any given range is plotted as if they all had the diameter of the middle of the... [Pg.26]

By carefully controlling the precipitation reaction we can significantly increase a precipitate s average particle size. Precipitation consists of two distinct events nu-cleation, or the initial formation of smaller stable particles of precipitate, and the subsequent growth of these particles. Larger particles form when the rate of particle growth exceeds the rate of nucleation. [Pg.240]

The beta particle formed when a neutron converts to a proton equivalent to an electron ( iP). [Pg.642]

Z-spray. Z refers to the approximate shape of the trajectory of particles formed by electrospray ionization... [Pg.447]

The capillary retention forces in the pores of the filter cake are affected by the size and size range of the particles forming the cake, and by the way the particles have been deposited when the cake was formed. There is no fundamental relation to allow the prediction of cake permeabiUty but, for the sake of the order-of-magnitude estimates, the pore size in the cake may be taken loosely as though it were a cylinder which would just pass between three touching, monosized spheres. If dis the diameter of the spherical particles, the cylinder radius would be 0.0825 d. The capillary pressure of 100 kPa (1 bar) corresponds to d of 17.6 pm, given that the surface tension of water at 20°C is 12.1 b mN /m (= dyn/cm). [Pg.389]

An expression for the number of particles formed during Stage I was developed, assuming micellar entry as the formation mechanism (13), where k is a constant varying from 0.37 to 0.53 depending on the relative rates of radical adsorption in micelles and polymer particles, r is the rate of radical generation, m is the rate of particle growth, is the surface area covered by one surfactant molecule, and S is the total concentration of soap molecules. [Pg.23]

In atomization, a stream of molten metal is stmck with air or water jets. The particles formed are collected, sieved, and aimealed. This is the most common commercial method in use for all powders. Reduction of iron oxides or other compounds in soHd or gaseous media gives sponge iron or hydrogen-reduced mill scale. Decomposition of Hquid or gaseous metal carbonyls (qv) (iron or nickel) yields a fine powder (see Nickel and nickel alloys). Electrolytic deposition from molten salts or solutions either gives powder direcdy, or an adherent mass that has to be mechanically comminuted. [Pg.182]

By-products of these reactions are reclaimed and recycled. The color depends on the size of the particles formed. Size is controlled by regulating the calcination profile, ie, time and temperature. The calcined product is ground, washed, and classified. [Pg.11]

Reverse cleaners operate on the same principles as forward cleaners (20). Contaminants less dense than water migrate toward the center of the cleaner and exit as a separate (reject) stream from the pulp slurry. Reverse cleaners are used to remove adhesive and plastic particles as well as paper filler particles and lightweight particles formed from paper coatings. [Pg.8]

If the dispersion particles are attracted to each other, they tend to flocculate and form a stmcture. At low concentrations the particles form open aggregates, which give a fractal stmcture (93,94). At higher concentrations a network stmcture results, which can be so pronounced that the mixture has a yield point and behaves like a soHd when at rest. Shearing breaks up this stmcture, and viscosity decreases. [Pg.174]

In order to obtain a homogenous and stable latex compound, it is necessary that insoluble additives be reduced in particle size to an optimum of ca 5 )Tm and dispersed or emulsified in water. Larger-size chemical particles form a nucleus for agglomeration of smaller particles and cause localized dispersion instabiHty particles <3 fim tend to cluster with similar effect, and over-milled zinc oxide dispersions are particularly prone to this. Water-soluble ingredients, including some accelerators, can be added directly to the latex but should be made at dilute strength and at similar pH value to that of the latex concentrate. [Pg.252]

In the typical flame or vapor-phase hydrolysis process, which uses SiCfy as the precursor, sihcon tetrachloride vapor is fed into a flame using an oxygen carrier gas. Fine (<50 nm), amorphous sihca particles form in the flame (57). [Pg.499]

In drying solutions or slurries of solutions, the location of the feed-injection nozzle (spray nozzle) has a great effecl on the size of particle formed in the bed. Also of importance are the operating temperature, relative humidity of the off gas, and gas velocity. Particle growth can occur as agglomeration or as an onion sldnuing. ... [Pg.1568]

Heywood [Heywood, Symposium on Paiticle Size Analysis, lust. Chem. Engrs. (1 7), Suppl. 25, 14] recognized that the word shape refers to two distinc t charac teiistics of a particle—form and proportion. The first defines the degree to which the particle approaches a definite form such as cube, tetr edron, or sphere, and the second by the relative proportions of the particle which distinguish one cuboid, tetrahedron, or spheroid from another in the same class. He replaced historical quahtative definitions of shape by numerical shape coefficients. [Pg.1825]

Spray Drying Detailed descriptions of spray dispersion dryers, together with apphcation, design, and cost information, are given in Sec. 17. Product quality is determined by a number of properties such as particle form, size, flavor, color, and heat stability. Particle size and size distribution, of course, are of greatest interest from the point of view of size enlargement. [Pg.1899]

FIGt 22-67 Fouling schematics. Case A—Particles plug narrow pores and narrow larger ones. Case B—Particles plug narrow pores. Case C—Particles form a layer on the membrane. Case D—Particles or debris plug the largest pores. [Couttesy Elsevier (modified).]... [Pg.2041]

Many hydrocarbon flames are luminous because of the incandescent carbon particles formed in the flames. Under certain conditions, these particles are released from the luminous flames as smoke. Smoke from hydrocarbons is usually formed when the system is fuel rich, either overall or locally. [Pg.2314]

Sulfate particles formed in the gas phase can condense. In addition, sulfate can become bound to metals and can be adsorbed on unburned carbon particles. [Pg.2382]

What are the two primary gaseous pollutants that transform to fine-particle form during long-range transport ... [Pg.39]


See other pages where Particle form is mentioned: [Pg.242]    [Pg.775]    [Pg.776]    [Pg.204]    [Pg.253]    [Pg.432]    [Pg.116]    [Pg.24]    [Pg.24]    [Pg.381]    [Pg.69]    [Pg.182]    [Pg.182]    [Pg.234]    [Pg.404]    [Pg.112]    [Pg.125]    [Pg.9]    [Pg.485]    [Pg.6]    [Pg.449]    [Pg.413]    [Pg.530]    [Pg.151]    [Pg.1208]    [Pg.1235]    [Pg.1705]    [Pg.1782]    [Pg.462]    [Pg.14]   
See also in sourсe #XX -- [ Pg.69 , Pg.256 ]




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