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Appendix D: Fluid Mechanics—Reviews

            of Selected Topics






            Fluid mechanics is pertinent in the design of nearly all unit  additive effect of this pressure profile, i.e., the integration of
            processes. Topics of particular interest include drag, pipe flow  the infinitesimal forces over the whole surface, causes a
            (incompressible and compressible), flow distribution by mani-  resultant force opposite to the plate velocity vector.
            folds, porous media flow, flow measurement, turbulence, and  The calculation of the drag of a body is given by
            dispersion. These areas are reviewed here to provide a ready
            reference for key equations and associated coefficients. In the                v  2
                                                                                  F D ¼ C D r  A            (D:1)
            case of compressible flow, the logic is outlined as well as the                 2
            final equations. The review is intended to provide reference
            for frequently sought equations, but may not be readily  in which
            accessible. The equations may also be useful for spreadsheet  F D is the drag force on body (N)
            applications.                                         C D is the coefficient of drag (dimensionless)
                                                                  A is the area of body projection perpendicular to the
                                                                                      2
                                                                    direction of motion (m )
            D.1 FLUID DRAG
                                                                  v o is the velocity of body relative to fluid (m=s)
                                                                                          2
            Drag is a fundamental notion of fluid mechanics and it per-  r is the density of fluid (kg=m )
            meates many kinds of problems. Examples include sedimen-
            tation, sediment transport, headloss in pipes, pump design,  Equation D.1 is applicable to both friction drag and form drag.
            airfoil design, design of mixers, energy dissipation, etc. Prob-  The coefficient, C D , is quite different in each case.
            lems of particular interest in unit operations include fall
            velocity of particles, paddle wheel design in flocculation,
                                                               D.1.2 FLOW REGIME
            mixing, etc.
                                                               The drag coefficient depends upon the shape of the body and
                                                               the Reynolds number, i.e., R,defined,
            D.1.1  DRAG EQUATIONS
            Drag occurs when a fluid in motion contacts a surface of a                   rvD
                                                                                                            (D:2)
            ‘‘body,’’ e.g., an impeller, a pipe wall, an airfoil, an automo-        R ¼  m
            bile, a solid particle settling in water, a gas bubble rising in
            water, ad infinitum. The two types of drag are friction drag  in which
            and form drag. Both occur in most situations and the total  R is the Reynolds number (dimensionless)
            drag on a ‘‘body’’ is the sum of the two.             v is the velocity of body relative to fluid (m=s)
              The friction drag is due to boundary layer shear. Headloss  D is the characteristic length (m)
                                                                                             2
            in a pipe, calculated by the Darcy–Weisbach equation is  m is the dynamic viscosity (N s=m )
            caused by friction drag. The resistance of an airfoil is due
            mostly to friction drag. The other kind of drag is form drag.  The length term, D, in Equation D.2 is selected to characterize
            The ‘‘lift’’ on an airfoil is due to form drag. A section of an  the system, e.g., pipe diameter, impeller diameter, etc. At low
            axial flow impeller is really an ‘‘airfoil’’ and the associated  Reynolds numbers, i.e., R < 10, the flow regime is laminar.
            pumping is due to lift. The pressure profile caused by flow  As R increases, the flow becomes transitional, and then as R
            around a body causes form drag (a ‘‘streamline’’ shape of an  increases further, the regime is fully turbulent. The specific
            object reduces form drag). The shape of the body determines  Reynolds number at each transition depends upon the kind of
            the pressure profile.                               shape.
              A flat rectangular plate provides a means to illustrate the
            two types of drag. If the plate is oriented with its surface
                                                               D.1.3 DRAG COEFFICIENTS
            parallel to the flow, the drag on the plate is caused by friction.
            If the plate is oriented with its surface perpendicular to the  As noted in Section D.1.2, drag coefficients depend on (1) the
            flow, the drag is caused by separation effects, called form  form (or shape) of the body and (2) the Reynolds number, R,
            drag. A pressure profile around the plate would show a nearly  associated with the velocity of the fluid. The drag coefficient,
            uniform positive pressure on the upstream face and a nearly  C D , must be determined by experiment, using a wind tunnel, a
            uniform negative pressure on the downstream face. The  towing tank, channel, or any other means to measure the drag

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