Page 313 - Air and Gas Drilling Manual
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7-22    Air and Gas Drilling Manual
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                                                     37 .
                                        f  =−  2 log           D e i     +  N 251 f        (7-70)
                                                              R
                                                                 
                                                                 
                               Equation 7-70 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
                                                           
                                                  1        
                                      f =                                            (7-71)
                                                  D 
                                                
                                           2 log.          
                                                   i
                                                      + 1 14
                                                  e    
                                                           
                               Equation 7-71 is valid for values of Reynolds numbers greater than 4,000.
                                   For follow-on calculations for flow in the drill string the absolute roughness for
                               commercial pipe, e p =  0.00015  ft,  will  be used for the inside  surfaces  of  the  drill
                               pipe and drill collars.
                                   Equation  7-67  together  with  Equations  7-68  through  7-71  can  be  used  in
                               sequential trial and error integration steps starting at the top of the inside of the drill
                               string (with the known exit pressure) and continuing for each subsequent change in
                               cross-sectional area inside the drill string until the pressure above the drill  bit  inside
                               the drill string is determined. These sequential change in  drill  string cross-sectional
                               area until the pressure at the bottom of the inside drill string is determined.
                                   The  mixture  of  incompressible  fluid  and  the  gas  passing  through  the  single
                               orifice has a high incompressible volume fraction and can, therefore, be assumed to
                               act physically as an incompressible mixture.    Thus,  borrowing  from  mud  drilling
                               technology, the pressure change through the drill bit, ∆P b, can be approximated by
                                                    w ˙  2
                                      ∆P =           t                                 (7-72)
                                        b                2
                                                       π
                                            2 g γ mixai  C 2     D bi 4
                                                       4
                               The  value  of  C  represents  the  aerated  fluid  flow  loss  coefficient  of  the  drill  bit
                               orifice.  Experiments have shown that aerated fluid flow is  ver complex.   The  gas
                               and incompressible fluid components in the aerated mixture appear to  alternate their
                               passage  through  the  orifice.    This  means  the  aerated  flow  through  the  orifice  is
                               inefficient.  The value of C for aerated fluid flow should  be taken as 0.70  to  0.85.
                               The pressure change obtained  from  Equation  7-72  is  subtracted  from  the  pressure
                               above the drill  bit  inside  the  drill  string  P ai  obtained  from  Equation  7-67.    The
                               annulus bottomhole pressure, P bh, is
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