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characterized by the fact that light gases are separated as soon as they are
            liberated (due to reduction in pressure). In other words, light components
            do not come into contact with heavier hydrocarbons; instead, they find
            their way out.
                 For flash separation, on the other hand, gases liberated from the oil
            are kept in intimate contact with the liquid phase. As a result,
            thermodynamic equilibrium is established between the two phases and
            separation takes place at the required pressure.
                 Comparing the two methods, one finds that in differential
            separation, the yield of heavy hydrocarbons (intermediate and heavy
            groups) is maximized and oil-volume shrinkage experienced by crude oil in
            the storage tank is minimized. This could be explained by the fact that
            separation of most of the light gases take place at the earlier high-pressure
            stages; hence, the opportunity of loosing heavy components with the light
            gases in low-pressure stages is greatly minimized. As a result, it may be
            concluded that flash separation is inferior to differential separation
            because the former experiences greater losses of heavy hydrocarbons that
            are carried away with the light gases due to equilibrium conditions.
            Nevertheless, commercial separation based on the differential concept is
            very costly and is not a practical approach because of the many stages
            required. This would rule out differential separation, leaving the flash
            process as the only viable scheme to affect gas–oil separation using a small
            number of stages. As illustrated in Table 1 [1], a close approach to
            differential separation is reached by using four to five flash separation
            stages. A comparison between the mechanisms of separation by the two
            methods is schematically simplified and presented in Table 2.



            3.4  METHODS OF SEPARATION
            The traditional process for recovering crude oil from high-pressure well
            streams is based on the flash separation concept explained in Section 3.3,

            Table 1  Flash and Differential Separation
                                  Percent approach
            No. of flash stages      to differential
            2                           0
            3                          75
            4                          90
            5                          96
            6                          98.5







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