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              Fluid Dynamics (Chemical Engineering)                                                        69






































                     FIGURE 11 Generalized correlation of drag coefficient for Herschel–Bulkley model fluids; Q is defined by Eq. (165)

                     and reduces to appropriate parameters for Bingham plastic, power law, and Newtonian fluid limits.

              where d p is the “effective” spherical diameter of the parti-  one to determine drag coefficients for spheres in a wide
              cle, v ∞ and ρ are as defined above, and µ is the viscosity  variety of non-Newtonian fluids.
              of the fluid. The effective spherical diameter is the diam-  The curve in Fig. 11 has been represented by the follow-
              eter of a sphere of equal volume. Also of importance are  ing set of empirical equations to facilitate computerization
              “shape” factors, which empirically account for the non-  of the iterative process of determining C D ,
              sphericity of real particles and for the much more complex


              flow distributions they engender.                              C D = 24/Q ,   Q ≤ 1         (166)
                Figure 11 is a plot of C D as a function of a generalized
                                                                            C D = exp[q(lnQ )],          (167)

              parameter Q ,defined by


                                                                where the function q(x) with x = ln (Q ) has the form
                                    Re 2                                                       2
                                      pHB                        q(x) = 3.178 − 0.7456x − 0.04684x
                        Q =                     ,      (165)
                             Re pHB + (7π/24)He pHB                              3          4
                                                                       + 0.05455x − 0.01796x
                                                                                                 −4
                                                                                 −3
              where Re pHB and He pHB are the Reynolds number and      + 2.4619(10 )x 5 x  − 1.1418(10 )x .  (168)
                                                                                                     6
              Hedstrom number, respectively, for the Herschel–Bulkley

              rheological model defined as in the pipe flow case with D  For Q > 1000, C D = 0.43 is used. In the Newtonian limit,
              replaced by d P .                                 Eq. (166) is Stokes’ law.
                This parameter is defined to accommodate Herschel–
              Bulkley model fluids. In the limit τ 0 = 0, it reduces to
              an equivalent power law particle Reynolds number. In the  SEE ALSO THE FOLLOWING ARTICLES
              limit n = 1, it reduces to a compound parameter involving
              theBinghamplasticparticleReynoldsnumberandparticle  FLUID DYNAMICS • FLUID MIXING • LIQUIDS,STRUC-
              Hedstrom number. In both limits it reduces to the Newto-  TURE AND DYNAMICS • REACTORS IN PROCESS ENGI-
              nian particle Reynolds number. This correlation permits  NEERING • RHEOLOGY OF POLYMERIC LIQUIDS
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