Page 105 - Compression Machinery for Oil and Gas
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94  SECTION   II Types of Equipment



                  1000
                  900
                  800
                  700
                Pressure (psia)  600  Mixed (Gas/liquid) phase  Gas phase

                  500
                  400
                  300
                  200
                  100
                    0
                           70      90    110
                     50                         130    150    170    190
                                           Temperature (°F)
                                       Gas dew line  Seal gas supply
            FIG. 3.61 Phase map of the seal gas and 20K margin to the expansion curve.


               In order to avoid condensation, the calculation of the expansion curve from
            the point the seal gas enters the support system all the way through the seal gap
            and comparison with the condensation curve in the phase map is mandatory. A
            minimum design margin of 20K is usually recommended to ensure the seal gas
            is gaseous, see Fig. 3.61. Additional cooling in the lines and supply channels
            must be considered. If a proper design margin cannot be maintained, it may
            be required to heat up the seal gas to maintain the specified design margin from
            dew point. Electrical heaters with Thyristor control utilizing silicon-controlled
            rectifiers (SCRs) can precisely control the heating load and hold the seal gas
            temperature.
               For mixtures with already small amounts of longer-chain hydrocarbons (C6
            +), the condensation limit shifts strongly in the direction of higher temperature.
            This can result in gas temperatures that exceed the design temperature of indi-
            vidual components downstream of the heater. For these cases, a cooler with a
            downstream separator is installed. Long-chain hydrocarbons condensate and
            get removed in the separator. A heater after the separator is then absolutely
            necessary.
               In cryogenic applications, increasing the seal gas temperature to provide
            higher margins from dew point may adversely impact the compressor perfor-
            mance, because of the main portion of warm seal gas (e.g., more than 90%)
            is circulated back to the compressor flow path through the process labyrinth
            at the back of the impellers.
               Fig. 3.62 shows a typical arrangement of the entirety of components that
            might be required for gas conditioning. After passing the conditioning unit,
            the seal gas gets throttled by means of the control valve and forwarded to
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