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Particle size measurement static

Particle size measurement is one of the essential requirements in almost all uses of colloids. However, our discussion in Section 1.5 makes it clear that this is no easy task, especially since even the definition of particle size is difficult in many cases. A number of techniques have been developed for measuring particle size and are well documented in specialized monographs (e.g., Allen 1990). Optical and electron microscopy described in the previous section can be used when ex situ measurements are possible or can be acceptable, but we also touch on a few nonintrusive methods such as static and dynamic light scattering (Chapter 5) and field-flow fractionation (see Vignette II Chapter 2) in other chapters. [Pg.45]

Indices are dimensionless parameters derived from various mechanical and physical properties of the tablet blend and resulting compacts. Mechanical properties typically measured include indentation hardness (kinetic and static), elastic modulus, and tensile strength (10,11). Physical properties include particle size, shape, and size distribution, density (true, bulk, and tapped), flow properties and cohesive properties. [Pg.376]

A commercially available 5% Pt/Al203 catalyst (Engelhard Industries 4759) was used in this study. The catalyst sample had a mean particle size of 55 pm as measured by light scattering, a BET surface area of 140 m2/g, a mean pore radius of 50 A and a density of 5.0 g/ml. The platinum loading was 4.65%, and the platinum dispersion was 0.28 as measured by static CO titration (ref. 11). [Pg.178]

The active pharmaceutical ingredient in a low-dose formulation is typically a small molecule, designed to meet a small particle size requirement for uniformity purposes, and can be susceptible to effects of static charge and segregation. The impact of static charge on the accuracy of blend uniformity measurements (i.e., sampling bias) is discussed in the next section. [Pg.125]

Malvern (Insitec) ECPS2 is designed to monitor and control particle size distributions from 0.5 to 1,500 pm, at concentrations up to 10,000 ppm, directly in pneumatic powder flow streams. Up to one thousand size distribution measurements per second are carried out at flow velocities from static to ultrasonic. Discrete data point, extracted from the log file, can be viewed. The data can also be viewed in tabular form and as a size distribution curve. Data can also be integrated over any selected range. A Statistical Process Control (SPC) option enables the file data to be viewed in standard control chart format either as an X or R chart. Various interface arrangements have been described, [203] ... [Pg.571]

Figure 8.28. Time dependence of the average particle size,D, during static annealing at 240°C, after melt mixing for 1 min. The slope 3 may be taken as a measure of the coalescence rate (see left). The coalescence rate vs. the residence time in the mixer t (right). Numbers indicate the blend composition as (PP + PP-MA)/aPA [Li et al., 1997]. Figure 8.28. Time dependence of the average particle size,D, during static annealing at 240°C, after melt mixing for 1 min. The slope 3 may be taken as a measure of the coalescence rate (see left). The coalescence rate vs. the residence time in the mixer t (right). Numbers indicate the blend composition as (PP + PP-MA)/aPA [Li et al., 1997].

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See also in sourсe #XX -- [ Pg.126 ]




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