Page 283 - Air and Gas Drilling Manual
P. 283

6-28    Air and Gas Drilling Manual
                                           64
                                      f =
                                                                                       (6-90)
                                           N
                                            R
                               This  equation  can  be  solved  directly  once  the  Reynolds  number  is  known.    In
                               general, Equation 6-90 is valid for values for Reynolds numbers from 0 to 2,000.
                                   The  empirical  expression  for  the  Fanning  friction  factor  for  transitional  flow
                               conditions is known as the Colebrook equation.  The Fanning friction factor cannot
                               be  determined  directly  and  must  be  solved  by  trial  and  error.    This  empirical
                               expression is
                                                                     
                                                       e             
                                       1               D −  D p   251  
                                                                    .
                                                       h
                                          =−  2 log           +                      (6-91)
                                        f              37 .      N  R  f  
                                                                       
                                                                       
                               where e is the absolute roughness of the annulus surface (ft).  In general, Equation 6-
                               94 is valid for values of Reynolds numbers from 2,000 to 4,000.
                                   The  empirical  expression  for  the  Fanning  friction  factor  for  turbulent  flow
                               conditions is known as the von Karman equation.  This empirical expression is
                                                                  2
                                                                
                                      f =          1                               (6-92)
                                                 D −  D       
                                                   h
                                                        p
                                                
                                                         
                                                           + 1 14
                                           2 log.               
                                                         
                                                
                                                     e
                                                                
                               In general, Equation 6-92 is valid for values of Reynolds numbers greater than 4,000.
                                   For follow-on calculations for flow in  the  annulus  the  absolute  roughness  for
                               commercial pipe, e p =  0.00015  ft,  will  be used for the outside surfaces of the drill
                               pipe and drill  collars, and inside surface of  the  casing.    The  openhole  surfaces  of
                               boreholes will be approximated with  an absolute roughness, e oh =  0.01  ft (i.e.,  this
                               example value is the same as concrete pipe which approximates borehole surfaces in
                               limestone  and  dolomite  sedimentary  rocks,  or  in  similar  competent  igneous  and
                               metamorphic rocks, see Table 8-1).
                                   Equation  6-88  together  with  Equations  6-89  through  6-92  can  be  used  in
                               sequential trial and error integration steps starting at the top of the annulus (with the
                               known exit pressure) and continuing for each subsequent  change  in  annulus  cross-
                               sectional area until the bottomhole pressure is determined.
                                   If the stable foam is not preformed at injection, the flow down the inside of the
                               drill  string  is  that  of  an  aerated  fluid  mixture.    Such  an  aerated  mixture  can  be
                               assumed to pass through the nozzles in much the same manner as an incompressible
                               fluid.  Thus, borrowing from mud  drilling  technology, the pressure change through
                               the drill bit, ∆P b, can be approximated by
   278   279   280   281   282   283   284   285   286   287   288