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Particle size, aggregates

Spray pyrolysis routes have been extensively investigated to prepare Pt-based catalysts. Typically, a liquid feed of metal precursor and carbon is atomized into an aerosol and fed into a continuous furnace to evaporate and heat-treat to form a collectable powder. The method has good control over final aggregate particle size and metal particle size distributions, as well as producing powder without further isolation or separation. Hampton-Smith et al. have reviewed efforts of Superior MicroPowder (now Cabot Fuel Cells) in this area. ... [Pg.12]

Figure 17 shows that a more uniform mass distribution can be achieved at higher filtration velocities, both for the low and the high porous material. Finally, Fig. 18 shows the utilized capacity of the filter wall for all the cases in study, computed with a gas temperature of 280°C and a primary and aggregate particle size of 20 and 90 nm, respectively, as a function of the Peclet number. It is seen (Fig. 18) that the more porous materials with a smaller wall thickness can attain a better usage of the capacity of the filter wall, when the Peclet number increases. [Pg.231]

For a cluster of n spheres of diameter d, de = nd. When the aggregate particle size is small, the Cunningham correction factor should be considered. [Pg.244]

There have been some efforts in slurry recycling to reduce CoO of CMP consumables. In a recent study [37], the effluent samples were characterized for pH, trace-metal levels, viscosity, specific gravity, mean aggregate particle size, and LPC (>1.0 rm) before and after depth (melt-blown polymeric media) filtration. The study showed that the use of a recycled fumed silica slurry (recycled five times) decreased the CMP removal rate and the coefficient of friction (COF) by 40%. A perfect relationship was observed between the removal rate and COF. It was concluded that the increase in mean aggregate particle size, which lowers the contact area between the abrasive particles and the wafer, had some impact on the removal rate data. In general, there is a stronger emphasis on slurry additives and chemical action in current CMP processing with much lower maximum defectivity performance specifications [2]. [Pg.594]

Describe the controlling features ofthe finished product. a. Degree of uniformity solution, aggregates, particle size, etc. [Pg.39]

Several factors originating from the chemical structure and property of the drug molecule, and from the physiology within the environment in the GI tract, affect the flow of molecules across the intestinal membrane. These factors include solubility, partition coefficient, pffa, molecular weight, molecular volume, aggregate, particle size, pH in the lumen and at the surface of the membrane, GI secretions, absorptive surface area, blood flow, membrane permeability and enzymes (for more factors, see Ungell 1997, and Table 4.8). Complete absorption occurs when the drug has a maximum permeability coefficient and maximum solubility at the site of absorption (Pade and Stavchansky 1998). [Pg.117]

Samples measuring 40 x 40 x 160 mm were made using steel fibers with copper covering. The reinforcement ratio p = 2%, aspect ratio L/d = 100, and maximum coarse aggregate particle size a = 5 mm conformed to the values obtained above. [Pg.73]

These values R are adduced in Table 6.1, from which their reduction in a sequence of technical carbon—nanoshungite—microshungite, that fully contradicts to the experimental data, i.e., to R change (Table 6.1). However, we must not neglect the fact that Eq. (6.14) was obtained within the frameworks of computer simulation, where the initial aggregating particle sizes are the same in all cases [31]. For real nanocomposites the values can be distinguished essentially (Table 6.1). It is expected that... [Pg.154]

The key feature of this mixture is that the aggregate particle size distribution curve presents a discontinuity between certain sieves. For this reason, FIRA is also known as gap-graded mixture. [Pg.268]

Particle Small spherical component of a carbon black aggregate produced by fracturing the aggregate. Particle size is measured by electron microscopy. [Pg.419]

In general the size of the pores depends, among other factors, on the particle size of the aggregate. Particle size is the most important parameter in the production of ceramic products it must be optimized to ensure that the desired mechanical and physical properties are achieved. The majority of ceramic products are manufactured by the process of slip casting in a mold. Maintenance of the desired PSD requires control of the dispersion stabUity of the ceramic shp. Like all ceramic materials and castables, in alumina refractories a proper PSD is of importance. [Pg.135]

Sedimentation employs the gravitational force acting on particles to achieve sohd— liquid separation. For most wastewater treatment apphcations, the use of sedimentation presupposes that the primary particles resident in a wastewater are destabilized and flocculated into an aggregate particle size and density that allows for effective removal. Stokes law provides a first-order estimate of the settling velocity and indicates that the vertically downward velocity increases as the square of the particle diameter, and in direct proportion to the density difference between the particles and water. In practice, particle/floc diameters generally need to be at least several tens of pm for effective sedimentation. [Pg.251]

Under practical conditions the strength of mortar (aggregate particle size < 4 mm) and concrete (aggregate particle size usually < 16 mm, < 32 mm or < 63 mm) is affected more particularly by the following factors type and quality of the cement water-cement ratio (proportions by weight). [Pg.489]

Microanalytical methods are frequently used to study blooming and contamination of polymer and rubber surfaces, the formation of aggregates, particle size, shape and distribution of fillers. Eor this purpose high magnification (e.g. 150x) optical microscopy is commonly used. Success of this operation is usually dependent on generation of high quality microtome sections of the sample. [Pg.471]

Figure 2.3.6 Dependence of aggregated particle size on rotation speed of anode disk at 1.0 A... Figure 2.3.6 Dependence of aggregated particle size on rotation speed of anode disk at 1.0 A...
Homogeneity Aggregates Particle Sizes Optimal Size for optics... [Pg.157]


See other pages where Particle size, aggregates is mentioned: [Pg.477]    [Pg.477]    [Pg.225]    [Pg.39]    [Pg.1974]    [Pg.537]    [Pg.468]    [Pg.1962]    [Pg.72]    [Pg.276]    [Pg.434]    [Pg.72]    [Pg.467]    [Pg.88]    [Pg.57]    [Pg.70]    [Pg.70]    [Pg.43]    [Pg.359]    [Pg.140]    [Pg.234]    [Pg.339]    [Pg.496]    [Pg.86]    [Pg.218]   


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Aggregated particles

Aggregating particles

Aggregation particle size distribution

Aggregation sizes

Particle aggregate

Particle size aggregation

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