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48                                            Part I Liquid Drilling Systems




          Illustrative Example 2.7 (Continued )
          In the open-hole/drill collar annulus:

                 v =       300      = 4:59 ft/s
                            2     2
                     2:448ð8:5 − 6:75 Þ
                N Re = 5,218, N Rec = 2,737, N Re < N Rec , turbulent flow
                C = 0:5589

                  a
                                     −0:2638
                                          = 0:008
                 f a = 0:0767ð0:5589 × 5,218Þ
                                      2
                Δp f =     0:008 × 0:6684 × 10:5 × 7:48  ð450Þ = 18 psi
                                              2      2 2
                     1421:22 × ð0:708 − 0:563Þ × ð0:708 − 0:563 Þ
          The total system pressure loss is
                     Δp d = 491 + 204 + 42 + 21 + 18 = 776 psi = 5,279 kPa



        The Generalized Pressure Loss Model
        The total parasitic pressure loss in a drilling circulation system includes
        the frictional pressure loss in the surface equipment Δp s , frictional pressure
        losses in the drill pipe Δp dp and drill collars Δp dc , and frictional pressure
        losses in the drill collar annulus Δp dca and the drill pipe annulus Δp dpa .If
        each term of the parasitic pressure loss is computed for the usual case of
        turbulent flow, examining the equations for turbulent flow yields
                                    Δp d = cq m                     (2.74)

        where m is a constant that theoretically has a value near 1.75 for turbu-
        lent flow, and c is a constant that depends on the mud properties and
        wellbore geometry. Considering that laminar flow may exist in some
        annular sections, the constant m may take a value less than 1.75.
           The values of c and m can be estimated by matching the calculated
                                            m
        pressure losses with the model Δp d = cq at two flow rates. At a given
        depth of interest, suppose pressure losses at flow rates q 1 and q 2 are calcu-
        lated as Δp d1 and Δp d2 , respectively. The values of c and m in the flow
        rate range can be determined by

                                          Δp d2
                                      log
                                          Δp d1
                                 m =                                (2.75)
                                           q 2
                                       log
                                           q 1
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