Page 101 - Petroleum and Gas Field Processing
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(diameter and seam-to-seam length) of a horizontal separator is
            determined as follows:
                 5. Assume various values for the separator diameter, D.
                 6. For each assumed value of D, determine the effective length, L g ,
                    that satisfies the gas capacity constraint from Eq. (19) and
                    calculate the seam-to-seam length, L s , from

                                   D
                         L s ¼ L g þ  ft                                 ð21Þ
                                   12
                 7. For each assumed value of D, determine the effective length, L o ,
                    that satisfies the liquid capacity constraint from Eq. (20) and
                    calculate the seam-to-seam length, L s , from

                              4
                         L s ¼ L o ft                                    ð22Þ
                              3

                 8. For each value of D used, compare the values of L g and L o to
                    determine whether the gas capacity constraint or the oil capacity
                    constraint governs the design of the separator. Of course, the
                    larger required length governs the design.
                 9. Select reasonable combinations of D and L s such that the
                    slenderness ratio SR is in the range of 3–5. The cost and
                    availability would then determine the final selection.
                 The above equations and sizing procedures are very sufficient for
            the determination of separator diameter and length as well as for the
            performance evaluation of existing separators. The students and
            practicing engineers should be familiar with such design equations and
            procedures before attempting the use of commercially available software.
            The retention time is an important parameter in designing gas–oil
            separators. It is best obtained from laboratory tests that simulate the
            field operating conditions. This, however, may not always be available. In
            such cases, experience and data from offset fields, if available, will be
            very valuable.
                 On the commercial side, computer programs for sizing gas–oil
            separators have been developed by Ellis Engineering Inc. [1]. Capacity
            curves based on computer programs have been introduced as well by
            Smith and Ellis [1]. These curves are suitable for preliminary sizing for
            estimating gas and liquid capacities.
                 For spherical separators, curves have been developed [5] for sizing
            gas capacity as illustrated by the diagram given in Figure 18.






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