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Chapter 9: Aerated Fluid Drilling    9-9
                                    V c is the critical concentration velocity (ft/sec),
                                    V t is the terminal velocity of the rock cuttings particle (ft/sec).
                                   It is tacitly assumed that if the incompressible drilling  fluid can carry the rock
                               cuttings on its own, then the injection of gas into  the fluid will  enhance the overall
                               carrying capacity of the aerated fluid.
                                   The critical concentration velocity is the additional velocity needed to  distribute
                               the  rock  cuttings  through  the  incompressible  drilling  fluid  at  a  predetermined
                               concentration factor.  The usual concentration factor is  0.04.   Therefore,  the critical
                               concentration velocity, V c, is
                                      V c                                                (9-2)
                                            ,
                                           3 600  C
                               where   is the instantaneous drilling rate (ft/hr or m/hr),
                                    C is the concentration factor (usually assumed to be 0.04).
                                   Equations 9-1 and 9-2 equation can be used with any consistent set of units.
                                 Terminal Velocities (English Units)
                                   For direct circulation operations the terminal velocity of the rock cutting particle
                               is assessed in the annulus section of the borehole where the cross-sectional area is the
                               largest.    The  terminal  velocity  will  depend  on  the  actual  flow  conditions  in  the
                               annulus section (i.e., whether the flow is laminar, transitional, or turbulent).
                                   Empirical data indicates that laminar flow conditions exist when the non-dimensional
                               Reynolds  number  for  the  flow  is between  0 and  2,000. The  empirical  relationship  for
                               the terminal velocity of a rock cutting particle in an annulus with laminar flow, V t1, is

                                            .
                                      V    0 0333  D 2  s  f                            (9-3a)
                                       t1         c
                                                         e
                               where V t1 is the terminal velocity of the particle in laminar flow (ft/sec),
                                    D c is the approximate diameter of the rock cutting particle (ft),
                                                                           3
                                    s is the specific weight of the solid rock cutting (lb/ft ),
                                                                                   3
                                    f is the specific weight of the incompressible drilling fluid (lb/ft ),
                                                                    2
                                    e is the effective absolute viscosity (lb-sec/ft ).
                                   Empirical  data  indicates  that  transition  flow  conditions  exist  when  the  non-
                               dimensional  Reynolds  number  for  the  flow  is  between  2,000  and  4,000.    The
                               empirical  relationship  for  the  terminal  velocity  of  a  rock  cutting  particle  in  an
                               annulus with transition flow, V t2, is
                                                             2
                                                             3
                                                      s    f
                                             .
                                      V t2  0 492  D c     1                            (9-4a)
                                                           3
                                                       f  e
                               where V t2 is the terminal velocity of the particle in transition flow (ft/sec).
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