Page 137 - Petroleum and Gas Field Processing
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centipoise and d m be the droplet diameter in micrometers, the above
            equation becomes
                                   6   2
                    ð  Þð3:281   10 d m Þ
                 u ¼               5
                      18ð2:088   10  Þ
                                      2    ft
                 u ¼ 2:864   10  8  ð  Þd m                               ð6Þ
                                           s
            or
                                      2    ft
                 u ¼ 1:787   10  6  ð 
Þd m                               ð7Þ
                                           s

            where
                  
 ¼ 
   
 o
                       w
            
 o and 
 w are the specific gravity of oil and water, respectively, u is the
            terminal settling velocity of the droplet (ft/s), d m is the diameter of the
            droplet (mm), and m is the viscosity of the continuous phase (cP).
                 Equation 6 [or Eq. (7)] shows that the droplet settling velocity is
            inversely proportional to the viscosity of the continuous phase. Oil
            viscosity is several magnitudes higher than the water viscosity. Therefore,
            the settling velocity of water droplets in oil is much smaller than the
            settling velocity of oil droplets in water. The time needed for a droplet to
            settle out of one continuous phase and reach the interface between the
            two phases depends on the settling velocity and the distance traveled by
            the droplet. In operations where the thickness of the oil pad is larger than
            the thickness of the water layer, water droplets would travel a longer
            distance to reach the water–oil interface than that traveled by the oil
            droplets. This, combined with the much slower settling velocity of the
            water droplets, makes the time needed for separation of water from oil
            longer than the time needed for separation of oil from water. Even in
            operations with a very high water–oil ratio, which might result in having
            a water layer that is thicker than the oil pad, the ratio of the thickness of
            the water layer to that of the oil pad would not offset the effect of
            viscosity. Therefore, the separation of water droplets from the continuous
            oil phase would always be taken as the design criterion for three-phase
            separators.
                 The minimum size of the water droplet that must be removed from
            the oil and the minimum size of the oil droplet that must be removed from
            the water to achieve a certain oil and water quality at the separator exit
            depend largely on the operating conditions and fluid properties. Results
            obtained from laboratory tests conducted under simulated field conditions






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