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Suspensions applications

Agitation levels 3 and 5 characterize most chemical process industries solids-suspension applications and are typically used for dissolving solids. Agitators capable of scale levels of 3 will Suspend all the solids of design settling velocity completely off the vessel bottom Provide slurry uniformity to at least 1 /3 of fluid-batch height Be suitable for slurry draw-off at low exit-nozzle elevations. [Pg.84]

Unlike extended release parenteral formulations (depot suspensions), application of low-water-solubility salts in oral extended release forms is not used commonly. This probably is due to the fact that for oral delivery, coated and matrix-type systems are easy to design and can generate release profiles that are manipulated more easily than powder systems. Therefore, although it is not impossible, selecting a salt form with low water solubility to achieve a desired extended release profile has not been reported frequently. [Pg.156]

One area for industrial studies is the whole area of slurry pipelines. Coal is by far the most common material in slurry pipelines, but other pipelines, but other pipelines include iron ore and potash. In large volume solid suspension applications, there is a considerable trade-off between volume of a tank, mixer horsepower, shape of a tank, and many other areas of cost consideration that are important in overall design. In addition to the tanks in these sorts of slurry systems, it must be capable of incorporating slurries into water or vice versa to either increase or decrease the solids concentration of a given system. [Pg.292]

Non-magnetic beads of a variety of matrices, ready for coupling by various chemistries to oligos, antibodies, antigens, or what-have-you, are available for column or suspension applications from Polymer Laboratories (www.polymerlabs.com). [Pg.933]

The petroleum industry suspension applications and problems have in common the same basic principles of colloid science that govern the nature, stability, and properties of suspensions. The widespread importance of suspensions in general and scientific interest in their formation, stability, and properties have precipitated a wealth of published literature on the subject. This chapter provides an introduction intended to complement the other chapters on suspensions in this book. A good starting point for further basic information, although focused on clays, is van Olphen s classic book, An Introduction to Clay Colloid Chemistry (I). There are several other good books on suspensions (2, 3), and most good colloid chemistry texts contain introductions to suspensions and some of their properties (4-8). [Pg.11]

Figure 13 (A) A typical specimen stub. (B) The initial stage of carbon suspension application. (C) The carbon covering the entire stub. (D) The particulate material adhering to the coated stub. Figure 13 (A) A typical specimen stub. (B) The initial stage of carbon suspension application. (C) The carbon covering the entire stub. (D) The particulate material adhering to the coated stub.
Kress, D.W. (2008).The history of barbed suture suspension Application, and visions for the future. In Simplified Facial Rejuvenation, Springer, Berlin Heidelberg, 247-256. [Pg.404]

Effect of twisting torque, Mjj. In the usual suspension applications, leaf springs may be subjected to twisting, for example, by an obstacle under one wheel of an axle. For the two springs studied here, the rate of twist is design (S) = 1.47 X 10 in-lb/radians and design (SS) = 1.23 x 10 in-lb/radians. [Pg.271]

As an example. Figure 22-3 illustrates the very strong function of power versus the ratio of the impeller diameter to the tank diameter (D/T) for a solids suspension application. The optimum D/T occurs at 0.35 for this application. The ordinate shows the power versus the power at the optimum D/T. On the right side of the graph, the circled value indicates a power of 1.6 times the optimum at a D/T of 0.5. The large impeller cuts off the axial circulation loop. [Pg.1336]

Figure 22-3 Relative power versus D/T for solid suspension applications there is a distinct minimum in power requirement at D/T = 0.35. Figure 22-3 Relative power versus D/T for solid suspension applications there is a distinct minimum in power requirement at D/T = 0.35.
Weetman, R. J. (1994). Development of an erosion resistant mixing impeller for large scale solid suspension applications with CFD comparisons, presented at the 8th European Conference on Mixing, Cambridge. [Pg.1352]

Reactor designation Power level range, Mw heat Fuel solution or suspension Application... [Pg.12]


See other pages where Suspensions applications is mentioned: [Pg.465]    [Pg.146]    [Pg.420]    [Pg.81]    [Pg.465]    [Pg.625]    [Pg.659]    [Pg.81]    [Pg.148]    [Pg.157]    [Pg.719]    [Pg.720]    [Pg.24]    [Pg.719]    [Pg.720]    [Pg.285]    [Pg.321]    [Pg.263]    [Pg.264]    [Pg.401]    [Pg.318]    [Pg.1334]   
See also in sourсe #XX -- [ Pg.297 ]




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