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Drag ratio number

A typical graph of drag ratio as a function of superficial air velocity is shown in Figure 5.5 in which each curve refers to a constant superficial liquid velocity. The liquids in question exhibited power law rheology and the corresponding values of the Metzner and Reed Reynolds numbers ReMR based on the superficial liquid velocity uL (see Chapter 3) are given. The following characteristics of the curves may be noted ... [Pg.191]

Fig. 2 Dependence of drag ratio on Reynolds number and power-law index for =0.5. [Replotted from Tripathi et al. (1994).]... Fig. 2 Dependence of drag ratio on Reynolds number and power-law index for =0.5. [Replotted from Tripathi et al. (1994).]...
Fig. 4 Representative results on drag ratio as a function of aspect ratio and Reynolds number in shear-thickening fluids ( = 1.4). Fig. 4 Representative results on drag ratio as a function of aspect ratio and Reynolds number in shear-thickening fluids ( = 1.4).
Fig. 5 Variation of drag ratio with particle Reynolds number and aspect ratio for =1.8. Fig. 5 Variation of drag ratio with particle Reynolds number and aspect ratio for =1.8.
Based on such analyses, the Reynolds and Weber numbers are considered the most important dimensionless groups describing the spray characteristics. The Reynolds number. Re, represents the ratio of inertial forces to viscous drag forces. [Pg.332]

The drag coefficients for disks (flat side perpendicular to the direction of motion) and for cylinders (infinite length with axis perpendicular to the direclion of motion) are given in Fig. 6-57 as a Function of Reynolds number. The effect of length-to-diameter ratio for cylinders in the Newton s law region is reported by Knudsen and Katz Fluid Mechanics and Heat Transfer, McGraw-Hill, New York, 1958). [Pg.677]

And introducing the ratio of accelerations, = ag/g, where indicates the relative strength of acceleration, ag, with respect to the gravitational acceleration g. This is known as the separation number. The LHS of equation 60 contains a Reynolds number group raised to the second power and the drag coefficient. Hence, the equation may be written entirely in terms of dimensionless numbers ... [Pg.295]

Setting An established analytical method consisting of the extraction of a drag and its major metabolite from blood plasma and the subsequent HPLC quantitation was precisely described in a R D report, and was to be transferred to three new labs across international boundaries. (Cf. Section 4.32.) The originator supplied a small amount of drug standard and a number of vials containing frozen blood plasma with the two components in a fixed ratio, at concentrations termed lo, mid, and hi. The report provided for evaluations both in the untransformed (linear/linear depiction)... [Pg.254]

With regard to the drag on a sphere moving in a Bingham plastic medium, the drag coefficient (CD) must be a function of the Reynolds number as well as of either the Hedstrom number or the Bingham number (7V Si = /Vne//VRe = t0d/fi V). One approach is to reconsider the Reynolds number from the perspective of the ratio of inertial to viscous momentum flux. For a Newtonian fluid in a tube, this is equivalent to... [Pg.359]

Figure 21. Ratio of drag coefficient to low Reynolds number drag coefficient, uB/umj- - 10 and 3. (From Glicksman et al 1993b.)... Figure 21. Ratio of drag coefficient to low Reynolds number drag coefficient, uB/umj- - 10 and 3. (From Glicksman et al 1993b.)...
The use of a Reynolds number based on relative velocity rather than superficial velocity in setting these limits was suggested by Horio (1990). In setting viscous or inertial limits, it is the interphase drag which is characterized as being dominated by viscous or inertial forces. The particle inertia is important even if the interphase drag is viscous dominated. This is because of the typically large solid-to-gas density ratio. [Pg.53]

The ratio between the bed and particle diameters and the Reynolds number based on bed diameter, superficial velocity, and solid density appear only in the modified drag expression, in which they are combined, see Eq. (40). These parameters form a single parameter, as discussed by Glicksman (1988) and other investigators. The set of independent parameters controlling viscous dominated flow are then... [Pg.53]


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