Page 541 - Standard Handbook Petroleum Natural Gas Engineering VOLUME2
P. 541

Flow of Fluids   495

                     pbrr = 14.7 psia

                     T, = 75°F

                     Tp = 105'F
                     S.G.p = 0.752
                      S.G.,  = 54"API

                      Q, = 480 bpd (std) q,,,   = 0 bpd (std)

                      4L=9,+90
                      pg = 0.020 cp (constant value)
                      a, = 28 dyn/cm

                      GLR = GOR = 3393 scf/bbl

                      Choose a commercial steel pipe.
                    Solutions

                       1. Determine  the specific gravity of the oil:

                           SG, =    141.5   -  -  141e5  -0.763
                                 131.5 +  API   131.5 + 54

                       2. Find the weight associated with  1 bbl  of  stock-tank liquid


                           m = SG,(350)( l+$0R)+SG0(350)(   1 + WoR WOR )+(0.0764)(GLR)(!3Gg)


                                           1                1
                             = 0.763(350)(%)   + 0.763(S50)(lco)   +0.0764(3393)(0.752)
                             = 462 IWstb of oil


                       3. Determine  the specific weight  of the liquid phase:

                                            1            WOR
                           yL = 6n'4~0( + WOR)'sGw(     1 + WOR)]
                                         1



                              = 47.6 Idft5
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