Page 166 - Fundamentals of Enhanced Oil and Gas Recovery
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154                                                                       Forough Ameli et al.




                                                   m s H s
                                         z 5                   2 h                    (5.81)
                                                 2
                                              πr h MT s 2 T R Þ
                                                    ð
                                                     α t 2 t i Þ
                                                      ð
                                                                                      (5.82)
                                              t Dz 5
                                                             2
                                                    ðz1hÞ=2
                   Removal of hot fluids in Boberg Lantz model:
                                  _
                                 Q 5 5:615q oh ρ C o 1 F WOR ρ C w ðT p 2 T R Þ       (5.83)
                                                o
                                                            w
                                   p
                   Q p is the rate of energy removal (Btu/d), T p is the average T of heated region,

                   adjusted for removal of hot fluids ( F), F WOR is the water-to-oil ratio, energy
                   removed by hot fluid in (t 2 t i ):
                                                      t _
                                                       Q dλ
                                                   1     p
                                                    ð
                                               δ 5                                    (5.84)
                                                   2   m s H s
                                                      t i
                                           T p 2 T R
                                    T Dp 5         5 T Dr T Dz 1 2 δÞ 2 δ             (5.85)
                                                             ð
                                           T s 2 T R
                                   T p 5 T R 1 T s 2 T R Þ T Dr T Dz 1 2 δÞ 2 δ       (5.86)

                                                              ð
                                             ð
                   Gas water production in Boberg Lantz model is as follows:
                                            _
                                           Q 5 q oh H ogv 1 H wrv                     (5.87)
                                             p

                                   H ogv 5 5:615ρ C o 1 F GOR C g ðT p 2 T R Þ        (5.88)
                                                 o
                                   H wrv 5 5:615 F WOR ðH wT 2 H wr Þ 1 F wv λ s Š    (5.89)
                                               ½
                where H wrv is the enthalpy of produced water (Btu/bbl), H ogv is the enthalpy of pro-
                duced oil and gas (Btu/stb), H wT is the enthalpy of saturated water at T (Btu/lbm),
                F GOR is the GOR (scf/stb), F WOR is the WOR (bbl/stb), F WV is the for water
                condensed from produced vapor (bbl/stb).
                   The amount of water condensed from vapor is determined by:

                                                          p wv
                                      F wv 5 0:0001356ð  Þ      F GOR                 (5.90)
                                                        p w 2 p wr
                where F wv is the WOR for water condensate from produced gas (bbl w@60 F/stb),
                p wv is the vapor pressure of water at hTi, p w is the BHP, p wr is the vapor pressure of
                water at T R , F GOR is the GOR (scf/stb).

                                                          p wv
                                      F wv 5 0:0001356ð  Þ      F GOR                 (5.91)
                                                        p w 2 p wr
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