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Particle size Rosin-Rammler distribution

In the applications of gas-solid flows, there are three typical distributions in particle size, namely, Gaussian distribution or normal distribution, log-normal distribution, and Rosin-Rammler distribution. These three size distribution functions are mostly used in the curve fitting of experimental data. [Pg.19]

For computations the physical properties are assumed to be constant. Particle sizes are discretized by 10 equal-weight cuts from the Rosin-Rammler distribution... [Pg.222]

Knudsen s model led to the prediction that, if linear kinetics were followed, the age at which 50% of the cement has hydrated is proportional to the fineness constant (or xj in the Rosin/Rammler distribution (equation 4.1) for parabolic kinetics, it predicted that this age is proportional to (K40). Evidence was presented in support of this conclusion for cements considered to follow linear kinetics. The theory did not predict any relation to the breadth of the particle size distribution, which is represented by the slope of the Rosin-Rammler curve. [Pg.240]

Cumulative distributions can be fitted by a linear function if the data fit a suitable mathematical fimction. This curve fitting gives no insight into the fundamental physics by which the particle size distribution was produced. Three common functions are used to linearize the cumulative distribution the normal distribution fimction, the log-normal distribution function, and the Rosin—Rammler distribution function. By far athe most commonly used is the log-normal distribution function. [Pg.67]

The pulverized coal was sieved to separate a 200x270 mesh (U.S. Standard sieves) fraction. The mean weight particle size was 62 ym and the dispersion parameter 8.4 according to the Rosin-Rammler distribution (15). The size graded particles were dried under vacuum at 338 K for 8 hours, then stored in a dessicator until used. [Pg.258]

The Rosin-Rammler distribution function is another equation widely used in particle size measurement. It is a two-parameter function, usually given as cumulative percentage oversize ... [Pg.47]

A most useful approach has been published by Hirleman et al. This consisted of an artificial "aerosol" made up of an array of chrome thin-film circles on a transparent glass substrate. This calibration reticle contains more than 10000 of these particles randomly positioned in an 8 mm circle to simulate a Rosin Rammler distribution of spherical particles. Versions are available with different Rosin Rammler parameters X and N, and at least two levels of obscuration. The continuous Rosin Rammler size distribution is approximated on the reticle by 24 discrete particle sizes ranging from 2 to 105 m depending on the individual reticle. Each reticle is individually certified. An example of the goodness of fit to the Rosin Rammler distribution is shown in Figure 7. Hirleman et al use the reticle to check the performance of a Malvern 2200 model. [Pg.117]

The functional form of this inner-feed particle size distribution cannot be rigorously computed at this time. Even so, it is reasonable to assume that it should resemble that of the particles entering the cyclone. Thus, if a Rosin-Rammler distribution described the feed size distribution, then the inner feed should have this same functional form. Many feeds can be represented by a distribution function that is identical in form to the grade-efficiency equation shown in Eq. (6.3.1) ... [Pg.135]

Size Distribution Relationships. Different models have been used to describe the size distribution of particles experiencing single and multiple fractures. A model based on fracture at the site of the weakest link and a distribution of weakest links in the system gave results that could be described as well by the Rosin-Rammler relation (56). The latter is based on the concept that fracture takes place at pre-existing flaws that are distributed randomly throughout the particle. [Pg.222]

This mathematical form of the size distribution does not take account of the fact that die particle size does not stretch over die range from minus to plus infinity but has a limited range, and a modification such as the empirical Rosin-Rammler (1933) equation... [Pg.202]

Equation (1.35b) shows that a linear relationship exists when ln[ln( 1 // )] is plotted against In d. From the slope and intercept of this straight line, a and fl can be determined, a and fl are typically obtained from the particle size distribution data based on sieve analyses. Table 1.5 provides a list of typical values of a and fl for some materials for the Rosin-Rammler density function with d in the function having the unit micrometers (/tm). [Pg.21]

Fig. 4.1 Rosin-Rammler plot of the particle size distribution of a typical Portland cement. 5 = specific surface area attributable to particles of size smaller than. v. Open circuit grinding based on the data of Sumner et al. (S25). Fig. 4.1 Rosin-Rammler plot of the particle size distribution of a typical Portland cement. 5 = specific surface area attributable to particles of size smaller than. v. Open circuit grinding based on the data of Sumner et al. (S25).
It is further observed that there is an empirical function that can describe the particle size distribution of the powders prepared by using mechanical milhng, which is the Rosin-Rammler equation. One of the modified forms of the equation is given by ... [Pg.198]

A hammer crusher was designed to liberate the coating from the plastic substrate. The size distribution of particles was analyzed and could be described by the Rosin-Rammler function model (26-28). [Pg.294]

The Rosin-Rammler fimction is widely used in particle size distribution characterization. It was introduced in comminution studies in 1933 (Harris, 1971/1972), but was also used to describe the particle size distribution of moon dust (Allen, 1981). Usually, it is a two-parameter function given as a cumulative percentage undersize (Svarovsky, 2000) ... [Pg.74]

An empirical function that has been observed to describe the particle size distribution of milled powders is the Rosin-Rammler equation. The equation has undergone a number of modifications one form is... [Pg.135]

Milling of coal or coke produces a powder called pulverized fuel which contains particles of a wide range of sizes. As we saw in Chapter 3, the distance at which a particle in a particle-laden jet will travel in a combustion chamber plays a role in the damping of the jet s turbulent energy. Therefore theoretical analysis of combustion must take the particle size distribution of the fuel into account. Pulverized fuel fineness is therefore an important parameter in the modeling of coal combustion. An analytical expression of particle size distribution that has found a wide application for expressing the fineness of pulverized fuel is the Rosin-Rammler relation. The relationship is given by (Field et al., 1964)... [Pg.143]

Most CFD providers track particles in the reactive flow field by solving the pertinent equations for the trajectory of a sfafisfically significant sample of individual particles that represents a number of the real particles with the same properties. For example, following the Rosin-Rammler size distribution (Figure 6.6), coal particles are tracked using a statistical trajectory model followed by the modeling of the kinetics of devolatilization and subsequent volatile and char combustion as discussed previously in this chapter (Figure 6.9). Models similar to the law presented earlier are used for droplet combustion of atomized fuel oil. [Pg.160]

Quite often the well-known Rosin-Rammler-Bennett (RRB) particle size distribution is assumed for comminuted materials, which uses log d for the horizontal / 100 ... [Pg.101]

If the exponential relationship established by Rosin, Rammler and Sperling is strictly conformed to, the distribution curve appears as a straight line which is characterized by two values, the equivalent particle size d and the uniformity coefficient n (Fig. 4), where d is the size corresponding to 36.8% (by weight) retained as residue on the sieve (oversize) and n is the tangent of the slope of the line. Particle size distribution diagrams are commercially available which are provided with scales on the vertical and horizontal axes enabling the values of n and of the specific surface of comminuted materials to be read. [Pg.101]

Figure 3.4.14 Example of an ideal particle size distribution curve according to the Rosin-Rammler-Sperling-Bennett (RRSB) function for n = 1.3 ... Figure 3.4.14 Example of an ideal particle size distribution curve according to the Rosin-Rammler-Sperling-Bennett (RRSB) function for n = 1.3 ...
Particle size analysis is performed by graphical and statistical methods. A widely used distribution curve is the Rosin-Rammler-SpeHing-Bennett function. [Pg.172]

Rosin-Rammler-Sperling-Bennett Particle Size Distribution... [Pg.92]

The Rosin-Rammler-Sperling-Bennett (RRSB) particle size distribution is widely used for coal characterization. The basic formulation is... [Pg.92]

The characteristics of other distributions that have been applied to aerosol particle size, such as the Rosin-Rammler, Nukiyama-Tanasawa, power law, exponential, and Khrgian-Mazin distributions are given in the appendix to this chapter. These distributions apply to special situations and And limited application in aerosol science. They (and the lognormal distribution) have been selected empirically to fit the wide range and skewed shape of most aerosol size distributions. [Pg.47]


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See also in sourсe #XX -- [ Pg.72 , Pg.108 ]




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