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separated from the separator are collected using a VRU. This approach is
            recommended for small-size oil leases handling small volume of fluids to
            be processed. The principles underlying the stabilization process are the
            same as for gas–oil separation covered in Chapter 3.


            7.2.2  Stabilization by Stripping
            The stripping operation employs a stripping agent, which could be either
            energy or mass, to drive the undesirable components (low-boiling-point
            hydrocarbons and hydrogen sulfide gas) out of the bulk of crude oil. This
            approach is economically justified when handling large quantities of fluid
            and in the absence of a VRU. It is also recommended for dual-purpose
            operations for stabilizing sour crude oil, where stripping gas is used for
            stabilization. Stabilizer-column installations are used for the stripping
            operations.


            7.3  TYPES OF STABILIZER EMPLOYING ENERGY AS A
                 STRIPPING AGENT

            Two basic types of trayed stabilizer are commonly used:
                    Conventional reflux types normally operate from 150 to 300 psia.
                    This type of stabilizer is not common in field installations. It is
                    more suitable for large central field processing plants.
                    Nonrefluxed stabilizers generally operate between 55 and 85 psia.
                    These are known as ‘‘cold feed’’ stabilizers. They have some
                    limitations, but they are commonly used in field installations
                    because of their simplicity in design and operation.



            7.4  NONREFLUXED STABILIZERS
            7.4.1  Introduction
            When hydrocarbon liquids are removed from the separators, the liquid is
            at its vapor pressure or bubble point. With each subsequent pressure
            reduction, additional vapors are liberated. Therefore, if the liquids were
            removed directly from a high-pressure separator into a storage tank,
            vapors generated would cause loss of lighter as well as heavier ones. This
            explains the need for many stages in a GOSP. Nevertheless, regardless of
            the number of stages used, some valuable hydrocarbons are lost with the
            overhead vapor leaving the last stage of separation or the stock tank.






 Copyright 2003 by Marcel Dekker, Inc. All Rights Reserved.
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