Page 45 - Standard Handbook Petroleum Natural Gas Engineering VOLUME2
P. 45

Basic  Principles, Definitions, and Data   33


                  where  (CN)  is  the  bubble-point pressure correlating number and  the  other
                  terms have geen previously defined.
                    Standing also presents  equations for; density correction for compressibility
                  of  liquids; density correction for thermal expansion of  liquids; apparent liquid
                  densities of  natural gases; effect of  condensate volume on the ratio of  surface
                  gas  gravity to  well  fluid  gravity; pseudo-critical constants of  gases and  con-
                  densate fluids; pseudo-liquid density of systems containing methane and ethane;
                  and pseudecritical  temperatures and pressures for heptane and heavier.
                    Beggs and Robinson [7] recently collected PVT data and presented a better esti-
                  mate of the dead oil viscosity as a function of temperature and oil specific gravity:
                    POD = lox - 1                                               (5-25)

                  where poD = viscosity  in cp of  the gas-free oil at temperature, T, and X = yT-l.IS3,
                  y  = loz, and Z = 3.0324 - 0.02023 yo, with T in "F and the oil gravity y in "API.
                  An expression was also given for the saturated oil viscosity, p, or live oil below
                  the bubblepoint which  results from a linear relationship between log poD and
                  log p for a given  value of dissolved gas, Rs:
                    P = A VBon                                                  (5-26)

                  where A  = 10.715 (Rs +
                        B  = 5.44(Rs + 150)-0.338
                       Rs = sd/STB
                  In the first book specifically for hand-held calculators, Hollo and Fifadara [32]
                  presented  programs  for  estimating  gas  deviation  factor  (based  on  data  of
                  Standing and Katz):

                    Z  = 1 + (A, + AJT,  + AJT,S)pR  + (A4+ AdTR)pR* + A,pR*/T,S   (5-27)

                  where pR=  0.27 P$ZTR          T,  = T/Tc              P,  = P/Pc
                        A, = 0.31506             A, = - 1.0467           A, = - 0.5783
                       A,  = 0.5353              A,  = - 0.6123          A,  = 0.6815

                  A program was  also presented to  calculate the  single-phase formation volume
                  factor using ,the correlation developed by  Standing:
                                         :1""         1.175

                                io4
                    Bo = 0.9'72 + 1.47 [ (R,)(   + I.,,,]                        (5-28)

                  where y,   = solution gas specific gravity
                        yo = stock tank  oil specific gravity (141.5/131.5  + "API)
                        T = temperature, "F
                       Rs = solution gas-oil ratio, scf/STB
                       Bo = single-phase formation volume factor, RB/STB
                     OAPI  = stock tank oil gravity, "API
                    In  1980 Vazquez  and Beggs  [33] published improved empirical correlations
                  for  some  of  the  commonly required  crude  oil  PVT  properties.  Their  study
                  utilized a much larger database than was  used in previous work  so  the results
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