Page 494 - Air and Gas Drilling Manual
P. 494

Chapter 10: Stable Foam drilling    10-19
                               example,  the  volumetric  flow  rate  of  the  incompressible  fluid  will  be  sought.
                               Therefore, the trial and error process requires the selection of the magnitude  of  the
                               volumetric flow rate of the incompressible fluid (water and surfactant), q w,    required
                               to yield a minimum kinetic energy per unit volume in  the annulus of approximately
                                       3
                               3.0  ft-lb/ft .  Also,  the minimum  annulus foam quality must  be greater  than  0.60.
                               This trial and error technique further requires that the upper limit pressures in each depth
                               interval of the annulus be selected so that the overall interval integrals are satisfied.
                                   Table 4-1 gives an  average  atmospheric  pressure  of  12.685  psia  for  a  surface
                               location  of  4,000  ft  above  sea  level  (mid  latitudes  North  America)  (also  see
                               Appendix D).   The actual atmospheric pressure  for  the  air  at  the  drilling  location
                               (that will be used by the compressor), P at, is
                                             .
                                      p at  12 685 psia
                                      P at  p 144
                                             at
                                                     2
                                                .
                                            ,
                                      P at  1 826 6 lb/ft abs
                               The actual atmospheric temperature of the air at the  drilling  location  (that  will  be
                               used by the compressor), T at, is
                                      t    60˚F
                                       at
                                      T at  t at  459 67
                                                   .
                                      T     519 67˚R
                                              .
                                       at
                               Thus, P g and T g become
                                                          2
                                      P g  P at  1 826 6 lb/ft abs
                                                 ,
                                                     .
                                      T g  T at  519 67˚R
                                                   .
                               Using Equation 4-11, the specific weight of the gas entering the compressor is
                                                     0
                                                   1
                                             (,827 ) ( . )
                                             1
                                       g
                                            (53 .36 ) (519 . )
                                                     67
                                                    3
                                           0 0659 lb/ft
                                            .
                                       g
                               Note  the  above  specific  weight  value  can  also  be  obtained  from  Figure  D-4  in
                               Appendix D.
   489   490   491   492   493   494   495   496   497   498   499